US6841502B2 - Bridged bi-aromatic ligands, catalysts, processes for polymerizing and polymers therefrom - Google Patents

Bridged bi-aromatic ligands, catalysts, processes for polymerizing and polymers therefrom Download PDF

Info

Publication number
US6841502B2
US6841502B2 US10/421,212 US42121203A US6841502B2 US 6841502 B2 US6841502 B2 US 6841502B2 US 42121203 A US42121203 A US 42121203A US 6841502 B2 US6841502 B2 US 6841502B2
Authority
US
United States
Prior art keywords
group
abf
mmol
mmao
ligand
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
US10/421,212
Other languages
English (en)
Other versions
US20040014950A1 (en
Inventor
Thomas R. Boussie
Oliver Brümmer
Gary M. Diamond
Christopher Goh
Anne M. LaPointe
Margarete K. Leclerc
James A. W. Shoemaker
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Dow Global Technologies LLC
Original Assignee
Symyx Technologies Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority to US10/421,212 priority Critical patent/US6841502B2/en
Application filed by Symyx Technologies Inc filed Critical Symyx Technologies Inc
Assigned to SYMYX TECHNOLOGIES, INC. reassignment SYMYX TECHNOLOGIES, INC. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: BOUSSIE, THOMAS R., GOH, CHRISTOPHER, SHOEMAKER, JAMES A.W., LECLERC, MARGARETE K., BRUMMER, OLIVER, DIAMOND, GARY M., LAPOINTE, ANNE M.
Publication of US20040014950A1 publication Critical patent/US20040014950A1/en
Priority to US10/957,036 priority patent/US7126031B2/en
Publication of US6841502B2 publication Critical patent/US6841502B2/en
Application granted granted Critical
Priority to US11/436,145 priority patent/US7241715B2/en
Priority to US11/775,095 priority patent/US7659415B2/en
Assigned to SYMYX SOLUTIONS, INC. reassignment SYMYX SOLUTIONS, INC. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: SYMYX TECHNOLOGIES, INC.
Assigned to FREESLATE, INC. reassignment FREESLATE, INC. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: SYMYX SOLUTIONS, INC.
Assigned to DOW GLOBAL TECHNOLOGIES LLC reassignment DOW GLOBAL TECHNOLOGIES LLC ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: FREESLATE, INC.
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F10/00—Homopolymers and copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/16—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
    • B01J31/22—Organic complexes
    • B01J31/2204—Organic complexes the ligands containing oxygen or sulfur as complexing atoms
    • B01J31/2208—Oxygen, e.g. acetylacetonates
    • B01J31/2226—Anionic ligands, i.e. the overall ligand carries at least one formal negative charge
    • B01J31/223—At least two oxygen atoms present in one at least bidentate or bridging ligand
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/16—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
    • B01J31/22—Organic complexes
    • B01J31/2204—Organic complexes the ligands containing oxygen or sulfur as complexing atoms
    • B01J31/2208—Oxygen, e.g. acetylacetonates
    • B01J31/2226—Anionic ligands, i.e. the overall ligand carries at least one formal negative charge
    • B01J31/2243—At least one oxygen and one nitrogen atom present as complexing atoms in an at least bidentate or bridging ligand
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/16—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
    • B01J31/22—Organic complexes
    • B01J31/2204—Organic complexes the ligands containing oxygen or sulfur as complexing atoms
    • B01J31/226—Sulfur, e.g. thiocarbamates
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C215/00—Compounds containing amino and hydroxy groups bound to the same carbon skeleton
    • C07C215/74—Compounds containing amino and hydroxy groups bound to the same carbon skeleton having hydroxy groups and amino groups bound to carbon atoms of six-membered aromatic rings of the same carbon skeleton
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C217/00—Compounds containing amino and etherified hydroxy groups bound to the same carbon skeleton
    • C07C217/78—Compounds containing amino and etherified hydroxy groups bound to the same carbon skeleton having amino groups and etherified hydroxy groups bound to carbon atoms of six-membered aromatic rings of the same carbon skeleton
    • C07C217/80—Compounds containing amino and etherified hydroxy groups bound to the same carbon skeleton having amino groups and etherified hydroxy groups bound to carbon atoms of six-membered aromatic rings of the same carbon skeleton having amino groups and etherified hydroxy groups bound to carbon atoms of non-condensed six-membered aromatic rings
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C323/00—Thiols, sulfides, hydropolysulfides or polysulfides substituted by halogen, oxygen or nitrogen atoms, or by sulfur atoms not being part of thio groups
    • C07C323/10—Thiols, sulfides, hydropolysulfides or polysulfides substituted by halogen, oxygen or nitrogen atoms, or by sulfur atoms not being part of thio groups containing thio groups and singly-bound oxygen atoms bound to the same carbon skeleton
    • C07C323/18—Thiols, sulfides, hydropolysulfides or polysulfides substituted by halogen, oxygen or nitrogen atoms, or by sulfur atoms not being part of thio groups containing thio groups and singly-bound oxygen atoms bound to the same carbon skeleton having the sulfur atom of at least one of the thio groups bound to a carbon atom of a six-membered aromatic ring of the carbon skeleton
    • C07C323/20—Thiols, sulfides, hydropolysulfides or polysulfides substituted by halogen, oxygen or nitrogen atoms, or by sulfur atoms not being part of thio groups containing thio groups and singly-bound oxygen atoms bound to the same carbon skeleton having the sulfur atom of at least one of the thio groups bound to a carbon atom of a six-membered aromatic ring of the carbon skeleton with singly-bound oxygen atoms bound to carbon atoms of the same non-condensed six-membered aromatic ring
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C37/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom of a six-membered aromatic ring
    • C07C37/01—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom of a six-membered aromatic ring by replacing functional groups bound to a six-membered aromatic ring by hydroxy groups, e.g. by hydrolysis
    • C07C37/055—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom of a six-membered aromatic ring by replacing functional groups bound to a six-membered aromatic ring by hydroxy groups, e.g. by hydrolysis the substituted group being bound to oxygen, e.g. ether group
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C37/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom of a six-membered aromatic ring
    • C07C37/62—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom of a six-membered aromatic ring by introduction of halogen; by substitution of halogen atoms by other halogen atoms
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C39/00—Compounds having at least one hydroxy or O-metal group bound to a carbon atom of a six-membered aromatic ring
    • C07C39/24—Halogenated derivatives
    • C07C39/367—Halogenated derivatives polycyclic non-condensed, containing only six-membered aromatic rings as cyclic parts, e.g. halogenated poly-hydroxyphenylalkanes
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C41/00—Preparation of ethers; Preparation of compounds having groups, groups or groups
    • C07C41/01—Preparation of ethers
    • C07C41/16—Preparation of ethers by reaction of esters of mineral or organic acids with hydroxy or O-metal groups
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C41/00—Preparation of ethers; Preparation of compounds having groups, groups or groups
    • C07C41/01—Preparation of ethers
    • C07C41/18—Preparation of ethers by reactions not forming ether-oxygen bonds
    • C07C41/26—Preparation of ethers by reactions not forming ether-oxygen bonds by introduction of hydroxy or O-metal groups
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C41/00—Preparation of ethers; Preparation of compounds having groups, groups or groups
    • C07C41/01—Preparation of ethers
    • C07C41/18—Preparation of ethers by reactions not forming ether-oxygen bonds
    • C07C41/30—Preparation of ethers by reactions not forming ether-oxygen bonds by increasing the number of carbon atoms, e.g. by oligomerisation
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C43/00—Ethers; Compounds having groups, groups or groups
    • C07C43/02—Ethers
    • C07C43/20—Ethers having an ether-oxygen atom bound to a carbon atom of a six-membered aromatic ring
    • C07C43/23—Ethers having an ether-oxygen atom bound to a carbon atom of a six-membered aromatic ring containing hydroxy or O-metal groups
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07D—HETEROCYCLIC COMPOUNDS
    • C07D209/00—Heterocyclic compounds containing five-membered rings, condensed with other rings, with one nitrogen atom as the only ring hetero atom
    • C07D209/56—Ring systems containing three or more rings
    • C07D209/80—[b, c]- or [b, d]-condensed
    • C07D209/82—Carbazoles; Hydrogenated carbazoles
    • C07D209/86—Carbazoles; Hydrogenated carbazoles with only hydrogen atoms, hydrocarbon or substituted hydrocarbon radicals, directly attached to carbon atoms of the ring system
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07F—ACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
    • C07F7/00—Compounds containing elements of Groups 4 or 14 of the Periodic Table
    • C07F7/003—Compounds containing elements of Groups 4 or 14 of the Periodic Table without C-Metal linkages
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07F—ACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
    • C07F9/00—Compounds containing elements of Groups 5 or 15 of the Periodic Table
    • C07F9/02—Phosphorus compounds
    • C07F9/28—Phosphorus compounds with one or more P—C bonds
    • C07F9/50—Organo-phosphines
    • C07F9/5022—Aromatic phosphines (P-C aromatic linkage)
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2531/00—Additional information regarding catalytic systems classified in B01J31/00
    • B01J2531/02—Compositional aspects of complexes used, e.g. polynuclearity
    • B01J2531/0261—Complexes comprising ligands with non-tetrahedral chirality
    • B01J2531/0266—Axially chiral or atropisomeric ligands, e.g. bulky biaryls such as donor-substituted binaphthalenes, e.g. "BINAP" or "BINOL"
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2531/00—Additional information regarding catalytic systems classified in B01J31/00
    • B01J2531/40—Complexes comprising metals of Group IV (IVA or IVB) as the central metal
    • B01J2531/46—Titanium
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2531/00—Additional information regarding catalytic systems classified in B01J31/00
    • B01J2531/40—Complexes comprising metals of Group IV (IVA or IVB) as the central metal
    • B01J2531/48—Zirconium
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2531/00—Additional information regarding catalytic systems classified in B01J31/00
    • B01J2531/40—Complexes comprising metals of Group IV (IVA or IVB) as the central metal
    • B01J2531/49—Hafnium
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2603/00—Systems containing at least three condensed rings
    • C07C2603/02—Ortho- or ortho- and peri-condensed systems
    • C07C2603/04—Ortho- or ortho- and peri-condensed systems containing three rings
    • C07C2603/06—Ortho- or ortho- and peri-condensed systems containing three rings containing at least one ring with less than six ring members
    • C07C2603/10—Ortho- or ortho- and peri-condensed systems containing three rings containing at least one ring with less than six ring members containing five-membered rings
    • C07C2603/12—Ortho- or ortho- and peri-condensed systems containing three rings containing at least one ring with less than six ring members containing five-membered rings only one five-membered ring
    • C07C2603/18—Fluorenes; Hydrogenated fluorenes
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2603/00—Systems containing at least three condensed rings
    • C07C2603/02—Ortho- or ortho- and peri-condensed systems
    • C07C2603/04—Ortho- or ortho- and peri-condensed systems containing three rings
    • C07C2603/22—Ortho- or ortho- and peri-condensed systems containing three rings containing only six-membered rings
    • C07C2603/24—Anthracenes; Hydrogenated anthracenes
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2603/00—Systems containing at least three condensed rings
    • C07C2603/56—Ring systems containing bridged rings
    • C07C2603/58—Ring systems containing bridged rings containing three rings
    • C07C2603/70—Ring systems containing bridged rings containing three rings containing only six-membered rings
    • C07C2603/74—Adamantanes
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F110/00—Homopolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
    • C08F110/04—Monomers containing three or four carbon atoms
    • C08F110/06—Propene
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F210/00—Copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
    • C08F210/02—Ethene
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F210/00—Copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
    • C08F210/16—Copolymers of ethene with alpha-alkenes, e.g. EP rubbers
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F212/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an aromatic carbocyclic ring
    • C08F212/02—Monomers containing only one unsaturated aliphatic radical
    • C08F212/04—Monomers containing only one unsaturated aliphatic radical containing one ring
    • C08F212/06—Hydrocarbons
    • C08F212/08—Styrene
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F4/00—Polymerisation catalysts
    • C08F4/42—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors
    • C08F4/44—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides
    • C08F4/60—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides together with refractory metals, iron group metals, platinum group metals, manganese, rhenium technetium or compounds thereof
    • C08F4/62—Refractory metals or compounds thereof
    • C08F4/64—Titanium, zirconium, hafnium or compounds thereof
    • C08F4/659—Component covered by group C08F4/64 containing a transition metal-carbon bond
    • C08F4/65908—Component covered by group C08F4/64 containing a transition metal-carbon bond in combination with an ionising compound other than alumoxane, e.g. (C6F5)4B-X+
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F4/00—Polymerisation catalysts
    • C08F4/42—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors
    • C08F4/44—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides
    • C08F4/60—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides together with refractory metals, iron group metals, platinum group metals, manganese, rhenium technetium or compounds thereof
    • C08F4/62—Refractory metals or compounds thereof
    • C08F4/64—Titanium, zirconium, hafnium or compounds thereof
    • C08F4/659—Component covered by group C08F4/64 containing a transition metal-carbon bond
    • C08F4/65912—Component covered by group C08F4/64 containing a transition metal-carbon bond in combination with an organoaluminium compound

Definitions

  • the present invention relates to ligands, complexes, compositions and/or catalysts that provide enhanced olefin polymerization capabilities.
  • the catalysts are based on bridged bi-aromatic ligands and metal precursor compositions and/or metal complexes including such ligands combined with activators (or co-catalysts).
  • the invention also relates to methods of polymerization, and in particular to a high-activity solution polymerization process.
  • the invention also relates to novel polymers and their preparation based on the use of these novel catalysts, including isotactic polypropylene and methods of preparing isotactic polypropylene.
  • Ancillary (or spectator) ligand-metal coordination complexes e.g., organometallic complexes
  • compositions are useful as catalysts, additives, stoichiometric reagents, monomers, solid-state precursors, therapeutic reagents and drugs.
  • Ancillary ligand-metal coordination complexes of this type can be prepared by combining an ancillary ligand with a suitable metal compound or metal precursor in a suitable solvent at a suitable temperature.
  • the ancillary ligand contains functional groups that bind to the metal center(s), remain associated with the metal center(s), and therefore provide an opportunity to modify the steric, electronic and chemical properties of the active metal center(s) of the complex.
  • Certain known ancillary ligand-metal complexes and compositions are catalysts for reactions such as oxidation, reduction, hydrogenation, hydrosilylation, hydrocyanation, hydroformylation, polymerization, carbonylation, isomerization, metathesis, carbon-hydrogen activation, carbon-halogen activation, cross-coupling, Friedel-Crafts acylation and alkylation, hydration, dimerization, trimerization, oligomerization, Diels-Alder reactions and other transformations.
  • ancillary ligand-metal complexes and compositions are in the field of polymerization catalysis.
  • the ancillary ligand typically offers opportunities to modify the electronic and/or steric environment surrounding an active metal center. This allows the ancillary ligand to assist in the creation of possibly different polymers.
  • Group 4 metallocene based single site catalysts are generally known for polymerization reactions. See, generally, “Chemistry of Cationic Dicyclopentadienyl Group 4 Metal-Alkyl Complexes”, Jordan, Adv. Organometallic Chem ., 1991, Vol. 32, pp. 325-153 and the references therein, all of which is incorporated herein by reference.
  • metallocene catalysts One application for metallocene catalysts is producing isotactic polypropylene.
  • An extensive body of scientific literature examines catalyst structures, mechanism and polymers prepared by metallocene catalysts. See, e.g., Resconi et al., “Selectivity in Propene Polymerization with Metallocene Catalysts,” Chem. Rev . 2000, 100, 1253-1345 and G. W. Coates, “Precise Control of Polyolefin Stereochemistry Using Single-Site Metal Catalysts,” Chem. Rev . 2000, 100, 1223-1252 and the references sited in these review articles.
  • Isotactic polypropylene has historically been produced with heterogeneous catalysts that may be described as a catalyst on a solid support (e.g., titanium tetrachloride and aluminum alkyls on magnesium dichloride). This process typically uses hydrogen to control the molecular weight and electron-donor compounds to control the isotacticity. See also EP 0 622 380, EP 0 292 134 and U.S. Pat. Nos. 4,971,936, 5,093,415, 4,297,465, 5,385,993 and 6,239,236.
  • This invention provides a resolution to these needs.
  • This invention discloses enhanced catalytic performances for olefin polymerization when certain ligands are employed in a catalyst, where the ligands are dianionic chelating ligands that can occupy up to four coordination sites of a metal atom and more specifically have a bridged-bis-bi-aryl structure.
  • some of the ligands, metal complexes and polymers disclosed herein are themselves novel.
  • compositions of this invention comprise a ligand and a metal precursor and optionally an activator.
  • the ligands and the method of making the ligands is also part of this invention.
  • the catalysts in some embodiments are compositions comprising the ligand and metal precursor, and optionally may additionally include an activator, combination of activators or activator package.
  • the catalysts are metal-ligand complexes and optionally may additionally include an activator, combination of activators or activator package.
  • the metal-ligand complexes of this invention can be characterized by the general formula: (4,2,O,S)ML n ′ (VI) where 4,2,O,S) is a dianionic ligand having at least 4 atoms that are oxygen or sulfur and chelating to the metal M at at least 2, more specifically 4, coordination sites through oxygen and/or sulfur atoms;
  • M is a metal selected from the group consisting of groups 3-6 and Lanthanide elements of the Periodic Table of Elements, more specifically, from group 4 (Hf, Zr and Ti);
  • L is independently selected from the group consisting of halide (F, Cl, Br, I), optionally substituted alkyl, alkenyl, alkynyl, heteroalkyl, heteroalkenyl, heteroalkynyl, aryl, heteroaryl, alkoxyl, aryloxyl, silyl, boryl, phosphino, amino, alkylthio, arylthio, nitro, hydrido,
  • a polymerization process for monomers.
  • the polymerization process involves subjecting one or more monomers to the catalyst compositions or complexes of this invention under polymerization conditions.
  • the polymerization process can be continuous, batch or semi-batch and can be homogeneous, supported homogeneous or heterogeneous.
  • Another aspect of this invention relates to arrays of ligands, metal precursors and/or metal-ligand complexes. These arrays are useful for the high speed or combinatorial materials science discovery or optimization of the catalyst compositions or complexes disclosed herein.
  • a method of producing isotactic polypropylene in a solution process is disclosed and is surprisingly tunable based on the polymerization conditions, activators and substituents on the catalyst.
  • Other polymerization processes that are tunable based on the same criteria are the copolymerization of ethylene and styrene (or substituted styrene) and ethylene and other alpha-olefins with high incorporation of styrene or the alpha-olefin.
  • non-metallocene group 4 complexes as polymerization catalysts for the production of isotactic polypropylene or other polymers.
  • FIG. 1 a is an X-ray crystal structure of the compound identified herein as C5 and FIG. 1 b is an alternate view of the same crystal structure.
  • FIG. 2 is a spectrum comparing various isotactic polypropylene polymers made in accord with this invention, some with regio-errors and others without detectible regio-errors.
  • R 1 , R 2 , R 3 , R 4 , and R 5 can be identical or different (e.g. R 1 , R 2 , R 3 , R 4 , and R 5 may all be substituted alkyls or R 1 and R 2 may be a substituted alkyl and R 3 may be an aryl, etc.).
  • Use of the singular includes use of the plural and vice versa (e.g., a hexane solvent, includes hexanes).
  • R group will generally have the structure that is recognized in the art as corresponding to R groups having that name.
  • the terms “compound” and “complex” are generally used interchangeably in this specification, but those of skill in the art may recognize certain compounds as complexes and vice versa.
  • representative certain groups are defined herein. These definitions are intended to supplement and illustrate, not preclude, the definitions known to those of skill in the art.
  • “Optional” or “optionally” means that the subsequently described event or circumstance may or may not occur, and that the description includes instances where said event or circumstance occurs and instances where it does not.
  • the phrase “optionally substituted hydrocarbyl” means that a hydrocarbyl moiety may or may not be substituted and that the description includes both unsubstituted hydrocarbyl and hydrocarbyl where there is substitution.
  • alkyl refers to a branched or unbranched saturated hydrocarbon group typically although not necessarily containing 1 to about 50 carbon atoms, such as methyl, ethyl, n-propyl, isopropyl, n-butyl, isobutyl, t-butyl, octyl, decyl, and the like, as well as cycloalkyl groups such as cyclopentyl, cyclohexyl and the like. Generally, although again not necessarily, alkyl groups herein may contain 1 to about 12 carbon atoms.
  • the term “lower alkyl” intends an alkyl group of one to six carbon atoms, specifically one to four carbon atoms.
  • Substituted alkyl refers to alkyl substituted with one or more substituent groups (e.g., benzyl or chloromethyl), and the terms “heteroatom-containing alkyl” and “heteroalkyl” refer to alkyl in which at least one carbon atom is replaced with a heteroatom (e.g., —CH 2 OCH 3 is an example of a heteroalkyl).
  • substituent groups e.g., benzyl or chloromethyl
  • heteroatom-containing alkyl and “heteroalkyl” refer to alkyl in which at least one carbon atom is replaced with a heteroatom (e.g., —CH 2 OCH 3 is an example of a heteroalkyl).
  • alkenyl refers to a branched or unbranched hydrocarbon group typically although not necessarily containing 2 to about 50 carbon atoms and at least one double bond, such as ethenyl, n-propenyl, isopropenyl, n-butenyl, isobutenyl, octenyl, decenyl, and the like. Generally, although again not necessarily, alkenyl groups herein contain 2 to about 12 carbon atoms.
  • the term “lower alkenyl” intends an alkenyl group of two to six carbon atoms, specifically two to four carbon atoms.
  • Substituted alkenyl refers to alkenyl substituted with one or more substituent groups
  • heteroatom-containing alkenyl and “heteroalkenyl” refer to alkenyl in which at least one carbon atom is replaced with a heteroatom.
  • alkynyl refers to a branched or unbranched hydrocarbon group typically although not necessarily containing 2 to about 50 carbon atoms and at least one triple bond, such as ethynyl, n-propynyl, isopropynyl, n-butynyl, isobutynyl, octynyl, decynyl, and the like. Generally, although again not necessarily, alkynyl groups herein may have 2 to about 12 carbon atoms.
  • the term “lower alkynyl” intends an alkynyl group of two to six carbon atoms, specifically three or four carbon atoms.
  • Substituted alkynyl refers to alkynyl substituted with one or more substituent groups
  • heteroatom-containing alkynyl and heteroalkynyl refer to alkynyl in which at least one carbon atom is replaced with a heteroatom
  • alkoxy intends an alkyl group bound through a single, terminal ether linkage; that is, an “alkoxy” group may be represented as —O-alkyl where alkyl is as defined above.
  • a “lower alkoxy” group intends an alkoxy group having one to six, more specifically one to four, carbon atoms.
  • aryloxy is used in a similar fashion, with aryl as defined below.
  • hydroxy refers to —OH.
  • alkylthio intends an alkyl group bound through a single, terminal thioether linkage; that is, an “alkylthio” group may be represented as —S-alkyl where alkyl is as defined above.
  • a “lower alkyl thio” group intends an alkyl thio group having one to six, more specifically one to four, carbon atoms.
  • arylthio is used similarly, with aryl as defined below.
  • thioxy refers to —SH.
  • allenyl is used herein in the conventional sense to refer to a molecular segment having the structure —CH ⁇ C ⁇ CH 2 .
  • An “allenyl” group may be unsubstituted or substituted with one or more non-hydrogen substituents.
  • aryl refers to an aromatic substituent containing a single aromatic ring or multiple aromatic rings that are fused together, linked covalently, or linked to a common group such as a methylene or ethylene moiety. More specific aryl groups contain one aromatic ring or two or three fused or linked aromatic rings, e.g., phenyl, naphthyl, biphenyl, anthracenyl, phenanthrenyl, and the like. In particular embodiments, aryl substituents have 1 to about 200 carbon atoms, typically 1 to about 50 carbon atoms, and specifically 1 to about 20 carbon atoms.
  • Substituted aryl refers to an aryl moiety substituted with one or more substituent groups, (e.g., tolyl, mesityl and perfluorophenyl) and the terms “heteroatom-containing aryl” and “heteroaryl” refer to aryl in which at least one carbon atom is replaced with a heteroatom (e.g., rings such as thiophene, pyridine, isoxazole, pyrazole, pyrrole, furan, etc. or benzo-fused analogues of these rings are included in the term “heteroaryl”).
  • multi-ring moieties are substituents and in such an embodiment the multi-ring moiety can be attached at an appropriate atom.
  • naphthyl can be 1-naphthyl or 2-naphthyl
  • anthracenyl can be 1-anthracenyl, 2-anthracenyl or 9-anthracenyl
  • phenanthrenyl can be 1-phenanthrenyl, 2-phenanthrenyl, 3-phenanthrenyl, 4-phenanthrenyl or 9-phenanthrenyl.
  • aralkyl refers to an alkyl group with an aryl substituent
  • aralkylene refers to an alkylene group with an aryl substituent
  • alkaryl refers to an aryl group that has an alkyl substituent
  • alkarylene refers to an arylene group with an alkyl substituent
  • halo and “halogen” are used in the conventional sense to refer to a chloro, bromo, fluoro or iodo substituent.
  • haloalkyl refers to an alkyl, alkenyl or alkynyl group, respectively, in which at least one of the hydrogen atoms in the group has been replaced with a halogen atom.
  • heteroatom-containing refers to a molecule or molecular fragment in which one or more carbon atoms is replaced with an atom other than carbon, e.g., nitrogen, oxygen, sulfur, phosphorus, boron or silicon.
  • heteroalkyl refers to an alkyl substituent that is heteroatom-containing
  • heterocyclic refers to a cyclic substituent that is heteroatom-containing
  • heteroaryl refers to an aryl substituent that is heteroatom-containing
  • heteroatom-containing When the term “heteroatom-containing” appears prior to a list of possible heteroatom-containing groups, it is intended that the term apply to every member of that group. That is, the phrase “heteroatom-containing alkyl, alkenyl and alkynyl” is to be interpreted as “heteroatom-containing alkyl, heteroatom-containing alkenyl and heteroatom-containing alkynyl.”
  • Hydrocarbyl refers to hydrocarbyl radicals containing 1 to about 50 carbon atoms, specifically 1 to about 24 carbon atoms, most specifically 1 to about 16 carbon atoms, including branched or unbranched, saturated or unsaturated species, such as alkyl groups, alkenyl groups, aryl groups, and the like.
  • lower hydrocarbyl intends a hydrocarbyl group of one to six carbon atoms, specifically one to four carbon atoms.
  • Substituted hydrocarbyl refers to hydrocarbyl substituted with one or more substituent groups
  • heteroatom-containing hydrocarbyl and heterohydrocarbyl refer to hydrocarbyl in which at least one carbon atom is replaced with a heteroatom
  • substituted as in “substituted hydrocarbyl,” “substituted aryl,” “substituted alkyl,” “substituted alkenyl” and the like, as alluded to in some of the aforementioned definitions, is meant that in the hydrocarbyl, hydrocarbylene, alkyl, alkenyl, aryl or other moiety, at least one hydrogen atom bound to a carbon atom is replaced with one or more substituents that are functional groups such as hydroxyl, alkoxy, alkylthio, phosphino, amino, halo, silyl, and the like.
  • substituted When the term “substituted” appears prior to a list of possible substituted groups, it is intended that the term apply to every member of that group. That is, the phrase “substituted alkyl, alkenyl and alkynyl” is to be interpreted as “substituted alkyl, substituted alkenyl and substituted alkynyl.” Similarly, “optionally substituted alkyl, alkenyl and alkynyl” is to be interpreted as “optionally substituted alkyl, optionally substituted alkenyl and optionally substituted alkynyl.”
  • divalent as in “divalent hydrocarbyl”, “divalent alkyl”, “divalent aryl” and the like, is meant that the hydrocarbyl, alkyl, aryl or other moiety is bonded at two points to atoms, molecules or moieties with the two bonding points being covalent bonds.
  • aromatic is used in its usual sense, including unsaturation that is essentially delocalized across multiple bonds, such as around a ring.
  • silyl refers to the —SiZ 1 Z 2 Z 3 radical, where each of Z 1 , Z 2 , and Z 3 is independently selected from the group consisting of hydride and optionally substituted alkyl, alkenyl, alkynyl, heteroatom-containing alkyl, heteroatom-containing alkenyl, heteroatom-containing alkynyl, aryl, heteroaryl, alkoxy, aryloxy, amino, silyl and combinations thereof.
  • boryl refers to the —BZ 1 Z 2 group, where each of Z 1 and Z 2 is as defined above.
  • phosphino refers to the group —PZ 1 Z 2 , where each of Z 1 and Z 2 is as defined above.
  • phosphine refers to the group: PZ 1 Z 2 Z 3 , where each of Z 1 , Z 3 and Z 2 is as defined above.
  • amino is used herein to refer to the group —NZ 1 Z 2 , where each of Z 1 and Z 2 is as defined above.
  • amine is used herein to refer to the group: NZ 1 Z 2 Z 3 , where each of Z 1 , Z 2 and Z 3 is as defined above.
  • saturated refers to lack of double and triple bonds between atoms of a radical group such as ethyl, cyclohexyl, pyrrolidinyl, and the like.
  • unsaturated refers to the presence of one or more double and triple bonds between atoms of a radical group such as vinyl, acetylide, oxazolinyl, cyclohexenyl, acetyl and the like.
  • the ligands that are suitable for use in the catalysts herein have several general, alternative descriptions.
  • the ligands are dianionic, chelating ligands that may occupy up to four coordination sites of a metal atom.
  • the ligands can also be described as diaionic ligands that, when chelated to a metal atom, form at least one or two seven member metalocycles (counting the metal atom as one member of the seven member ring).
  • the ligands can be described as dianionic, chelating ligands that use either oxygen or sulfur as binding atoms to the metal atom.
  • the ligands can be described as non-metallocene ligands that can coordinate in an approximate C 2 -symmetcial complex with a metal atom. These embodiments can be used together or separately.
  • a base may be reacted with the ligand to form a salt, the product of which may then be reacted with a metal precursor (as described herein).
  • a metal precursor as described herein.
  • at least two of X, X′, Y and Y′ or at least two of X′′, X′′′, Y and Y′ have at least one hydrogen atom.
  • R 30 is selected from the group consisting of hydride and optionally substituted alkyl, alkenyl, alkynyl, heteroalkyl, heteroalkenyl, heteroalkynyl, aryl, heteroaryl, alkoxyl, aryloxyl, silyl, boryl, phosphino, amino, thioxy, alkylthio, arylthio, halide, nitro, and combinations thereof.
  • X and X′ are independently selected from the group consisting of oxygen, sulfur and —NR 30 —; and in still other embodiments X and X′ are independently selected from the group consisting of oxygen and sulfur.
  • Y and Y′ are selected from the group consisting of amino, hydroxy, alkoxy, aryloxy, thioxy, alkylthio and arylthio; and in still other embodiments Y and Y′ are independently selected from the group consisting of hydroxy and thioxy.
  • the “upper aromatic ring” is the ring to which a Y group (such as Y, Y′) is bonded or part of.
  • the “lower aromatic ring” is the ring to which an X group (such as X, X′, X′′, etc.) is bonded or part of.
  • at least one AR is a heteroaromatic and more specifically a heteroaryl group.
  • at least one upper aromatic ring is a heteroaromatic and more specifically a heteroaryl.
  • Other embodiments include those where at least one lower aromatic ring is a heteroaromatic and more specifically a heteroaryl.
  • the bridging group B is selected from the group consisting of optionally substituted divalent hydrocarbyl and divalent heteroatom containing hydrocarbyl. In other embodiments, B is selected from the group consisting of optionally substituted divalent alkyl, alkenyl, alkynyl, heteroalkyl, heteroalkenyl, heteroalkynyl, aryl, heteroaryl and silyl.
  • B can be represented by the general formula —(Q′′R 40 2 ⁇ z′′ ) z′ — wherein each Q′′ is either carbon or silicon and each R 40 may be the same or different from the others such that each R 40 is selected from the group consisting of hydride and optionally substituted hydrocarbyl, and optionally two or more R 40 groups may be joined into a ring structure having from 3 to 50 atoms in the ring structure (not counting hydrogen atoms); and z′ is an integer from 1 to 10, more specifically from 1-5 and even more specifically from 2-5 and z′′ is 0, 1 or 2. For example, when z′′ is 2, there is no R 40 groups associated with Q′′, which allows for those cases where one Q′′ is multiply bonded to a second Q′′.
  • R 40 is selected from the group consisting of hydride, halide, and optionally substituted alkyl, alkenyl, alkynyl, heteroalkyl, heteroalkenyl, heteroalkynyl, aryl, heteroaryl, alkoxyl, aryloxyl, silyl, boryl, phosphino, amino, thioxy, alkylthio, arylthio, and combinations thereof.
  • Specific B groups within these embodiments include —(CH 2 ) 2 —, —(CH 2 ) 3 —, —(CH 2 ) 4 —, and —(CH 2 )—(C 6 H 4 )—(CH 2 )—.
  • Other specific bridging moieties are set forth in the example ligands and complexes herein.
  • the ligands can be characterized by the general formula: wherein each of R 1 , R 2 , R 3 , R 4 , R 5 , R 6 , R 7 , R 8 , R 9 , R 10 , R 11 , R 12 , R 13 , R 14 , R 15 , R 16 , R 17 , R 18 , R 19 , and R 20 is independently selected from the group consisting of hydride, halide, and optionally substituted hydrocarbyl, heteroatom-containing hydrocarbyl, alkoxy, aryloxy, silyl, boryl, phosphino, amino, thioxy, alkylthio, arylthio, nitro, and combinations thereof; optionally two or more R groups can combine together into ring structures (for example, single ring or multiple ring structures), with such ring structures having from 3 to 12 atoms in the ring (not counting hydrogen atoms); B is a bridging group having from one to 50 atoms (not
  • the notation —Y, —Y′, —X and —X′ is intended to mean that the group can be part of the aromatic ring (forming a heteroaryl) and/or replace one or more of the R groups (R 1 -R 20 ).
  • the notation for the bridging group B ( ⁇ B ⁇ ) can be combined with either or both —X and —X′ or the bridging group can replace one or more of the R groups on the indictated structure (e.g., such as R 9 and/or R 19 ).
  • X and X′ are defined as X′′ and X′′′, above.
  • each of R 1 , R 2 , R 3 , R 4 , R 5 , R 6 , R 7 , R 8 , R 9 , R 10 , R 11 , R 12 , R 13 , R 14 , R 15 , R 16 , R 17 , R 18 , R 19 , and R 20 is independently selected from the group consisting of hydride, halide, and optionally substituted alkyl, heteroalkyl, aryl, heteroaryl, alkoxyl, aryloxyl, silyl, boryl, phosphino, amino, thioxy, alkylthio, arylthio, nitro, and combinations thereof.
  • each of R 1 , R 2 , R 3 , R 4 , R 5 , R 6 , R 7 , R 8 , R 9 , R 10 , R 11 , R 12 , R 13 , R 14 , R 15 , R 16 , R 17 , R 18 , R 19 and R 20 is independently selected from the group consisting of hydride, halide, and optionally substituted alkyl, heteroalkyl, aryl, heteroaryl, alkoxyl, aryloxyl, silyl, amino, alkylthio and arylthio.
  • at least one of R 2 and R 12 is not hydrogen and in still other embodiments both R 2 and R 12 are not hydrogen.
  • the ligands useful in this invention can be characterized by the formula: wherein R 2 , R 3 , R 4 , R 5 , R 6 , R 7 , R 8 , R 9 , R 12 , R 13 , R 14 , R 15 , R 16 , R 17 , R 18 , and R 19 are as defined above, B is as defined above, X and X′ are as defined above, and Y and Y′ are as defined above with the proviso that each of Y and Y′ include hydrogen.
  • the ligands useful in this invention can be characterized by the formula:
  • the bridging group has been made part of the X moieties and the bis-aryl moieties have been made the same as each other.
  • the Y moieties again include hydrogen.
  • each of R 2 , R 3 , R 4 , R 5 , R 6 , R 7 , R 8 and R 9 is independently selected from the group consisting of hydride, halide, and optionally substituted alkyl, alkenyl, alkynyl, heteroalkyl, heteroalkenyl, heteroalkynyl, aryl, heteroaryl, alkoxyl, aryloxyl, silyl, boryl, phosphino, amino, thioxy, alkylthio and arylthio, nitro, and combinations thereof.
  • the choice of X, X′, Y, Y′, R 2 , R 12 and B have a strong influence on the production of isotactic polypropylene in a solution process.
  • Specific ligands within the scope of this particularization include for example: LL1-LL10, LL12-LL23, LL26-LL32, LL37-LL40, LL45-LL49 and LL52-LL57.
  • R 2 and R 12 are bulky substituents and may be independently selected from the group consisting of optionally substituted cycloalkylaryl, aryl and heteroaryl. More specifically, each R 2 and/or R 12 is independently selected from the group consisting of optionally substituted aryl and heteroaryl.
  • R 2 and/or R 12 groups include carbozole, 3,5-bis-tert-butyl-phenyl, 1,2,3,4,5,6,7,8-octahydroanthacenyl, 1-naphthyl, 9-anthracenyl and 2,4,6-trimethylphenyl.
  • Specific ligands within the scope of this particularization for bulky substituents include:
  • the size and identity of the substituents on the upper aromatic ring has an influence on the production of isotactic polypropylene in a solution process, allowing for a range of isotactic polypropylene polymers to be prepared with desired properties.
  • R 7 and R 17 may be independently selected from the group consisting of halo and optionally substituted hydrocarbyl, alkoxy, aryloxy, dialkyl- or diarylamino, alkyl or arylthio.
  • R 4 and R 14 may be independently selected from the group consisting of halo and optionally substituted hydrocarbyl, alkoxy, aryloxy, dialkyl- or diarylamino, alkyl- or arylthio.
  • Specific ligands within the scope of this particularization include:
  • ligands are novel compounds and those of skill in the art will be able to identify such compounds from the above. Also, certain embodiments of these ligands are preferred for the polymerization of certain monomers in a catalytic composition and/or in a metal complex. These certain embodiments are discussed further below.
  • the ligands of the invention may be prepared using known procedures. See, for example, Advanced Organic Chemistry, March, Wiley, N.Y. 1992 (4 th Ed.). Specifically, the ligands of the invention may be prepared using a variety of synthesis routes, depending on the variation desired in the ligand. In general, building blocks are prepared that are then linked together with a bridging group. Variations in the R group substituents can be introduced in the synthesis of the building blocks. Variations in the bridge can be introduced with the synthesis of the bridging group.
  • each of the optionally substituted phenyl rings is prepared as a separate building block (schemes 1 (a and b) and 2).
  • the desired optionally substituted phenyls are then combined into bi-phenyl building blocks (schemes 3 and 4), which are then bridged together (schemes 7, 8, 9, and 10).
  • the optionally substituted phenyl building blocks are bridged together (schemes 5 and 6) and then additional optionally substituted phenyl building blocks are added to form the bridged bi-aryl structures (schemes 11, 12, 13, and 14).
  • schemes to effect certain substitutions on the phenyl groups are included (schemes 15, 16, 17 and 18).
  • cross coupling reactions are used (e.g., Suzuki, Negishi or Buchwald-Hartwig cross coupling). These cross coupling reactions are generally known in the art; for example, see Tetrahedron , 1998, 54(3/4), 263-303 and J. Am. Chem. Soc . 2001, 123(31), 7727-7729.
  • the starting materials or reagents used in these schemes are generally commercially available, or are prepared via routine synthetic means.
  • the symbol depicts a bridging moiety as defined elsewhere in this specification.
  • the term “upper phenyl ring” is used consistently with the term “upper aromatic ring”, described above.
  • the term “lower phenyl ring” is used consistently with the term “lower aromatic ring”, described above.
  • Scheme 1 a is a general building block synthesis scheme, specifically depicting the synthesis of Y-protected, 2-bromo substituted, upper phenyl ring building blocks:
  • a protecting group is used to prepare the appropriate building block (BB(a)).
  • the substituents on the building block are as defined above.
  • the variables R and R′ are generally selected from the same group as R 2 , and may be optionally substituted alkyl, aryl, amino and the like; optionally R and R′ may be linked or fused.
  • “Appropriate cross-coupling reaction conditions” are generally known to those of skill in the art, and may be found in the above-cited references. Other reaction conditions will be known to those of skill in the art, with reference to the examples herein.
  • Scheme 1b shows a general synthesis scheme for Y-protected, 2-bromo substituted, upper phenyl ring building blocks:
  • the variables are defined as discussed above.
  • Scheme 2 is a general scheme for the synthesis of X-protected 2-boronic ester substituted lower phenyl ring building blocks, X-protected 2-ZnCl substituted lower-ring building blocks, and X-deprotected 2-boronic acid substituted lower ring building blocks:
  • cat. H + refers to an acid catalyzed reaction that supplies a hydrogen ion, such as p-toluenesufonic acid (TsOH) or hydrochloric acid (HCl), as is known to those of skill in the art.
  • TsOH p-toluenesufonic acid
  • HCl hydrochloric acid
  • Scheme 3 is a general scheme for the synthesis of Y-protected upper phenyl ring, X-deprotected lower phenyl ring building block: In scheme 3, the variables are defined as discussed above.
  • Scheme 4 is a general scheme for the synthesis of 2-bromo substituted, Y-protected upper phenyl ring, X-deprotected lower phenyl ring building block:
  • the variables are defined as discussed above.
  • Scheme 5 is a general scheme for the synthesis of symmetric 2-Br substituted, 2-boronic ester-substituted and 2-ZnCl-substituted, bridged lower phenyl ring building blocks:
  • base refers to bases in general (such as cesium carbonate or potassium tert-butoxide), as is known to those of skill in the art.
  • cat. Pd(0) refers to a catalyst that uses a ligand-stabilized Pd 0 complex, known to those of skill in the art.
  • Scheme 6 is a general scheme for the synthesis of unsymmetric 2-Br substituted, 2-boronic ester-substituted and 2-ZnCl-substituted, bridged lower phenyl ring building blocks:
  • the variables are defined as discussed above.
  • Scheme 7 is a general scheme for the synthesis of symmetric Y-protected, upper phenyl ring 2-bromo-substituted, lower phenyl ring bridged building blocks: In scheme 7, the variables are defined as discussed above.
  • Scheme 8 is a general scheme for the synthesis of unsymmetric Y,Y′-protected, upper phenyl ring 2-bromo-substituted, lower phenyl ring bridged building blocks: In scheme 8, the variables are defined as discussed above.
  • Scheme 9 is a general scheme for the double reaction of building block BB(e) with bridge, followed by deprotection:
  • the variables are defined as discussed above.
  • Scheme 10 is a general scheme for the sequential reaction of building blocks BB(e) and BB(f) with bridge, followed by deprotection:
  • the variables are defined as discussed above.
  • Scheme 11 is a general scheme for the conversion of building block BB(a) to a boronic ester or ZnCl derivative, followed by double cross-coupling with building block BB(g) and subsequent deprotection:
  • the variables are defined as discussed above.
  • Scheme 12 is a general scheme for the conversion of building block BB(a) to a boronic ester or ZnCl derivative, followed by double cross-coupling with building block BB(j) and subsequent deprotection:
  • the variables are defined as discussed above.
  • Scheme 13 is a general scheme for the double cross-coupling of building blocks BB(h) or BB(i) with building block BB(a), followed by deprotection:
  • the variables are defined as discussed above.
  • Scheme 14 is a general scheme for the double cross-coupling of building blocks BB(k) or BB(l) with building block BB(a), followed by deprotection:
  • the variables are defined as discussed above.
  • Scheme 15 is a general scheme for the double cross-coupling of building block BB(m), followed by deprotection:
  • the variables are defined as discussed above.
  • Scheme 16 is a general scheme for the double cross-coupling of building block BB(n), followed by deprotection:
  • the variables are defined as discussed above.
  • the metal precursors are activated metal precursors, which refers to a metal precursor (described below) that has been combined or reacted with an activator (described below) prior to combination or reaction with the ancillary ligand.
  • the ligands of this invention will be combined with a metal compound or precursor and the product of such combination is not determined, if a product forms.
  • the ligand may be added to a reaction vessel at the same time as the metal or metal precursor compound along with the reactants, activators, scavengers, etc.
  • the ligand can be modified prior to addition to or after the addition of the metal precursor, e.g. through a deprotonation reaction or some other modification.
  • the metal precursor compounds may be characterized by the general formula M(L) n where M is a metal selected from the group consisting of groups 3-6 and Lanthanide elements of the Periodic Table of Elements, more specifically, from group 4 (Hf, Zr and Ti); L is independently selected from the group consisting of halide (F, Cl, Br, I), optionally substituted alkyl, alkenyl, alkynyl, heteroalkyl, heteroalkenyl, heteroalkynyl, aryl, heteroaryl, alkoxyl, aryloxyl, silyl, boryl, phosphino, amino, thioxy, alkylthio, arylthio, hydrido, allyl, diene, phosphine, carboxylates, 1,3-dionates, oxalates, carbonates, nitrates, sulphates, ethers, thioethers and combinations thereof; L may also be
  • n 1, 2, 3, 4, 5, or 6.
  • the metal precursors may be monomeric, dimeric or higher orders thereof.
  • titanium, hafnium and zirconium precursors include, but are not limited to TiCl 4 , Ti(CH 2 Ph) 4 , Ti(CH 2 CMe 3 ) 4 , Ti(CH 2 SiMe 3 ) 4 , Ti(CH 2 Ph) 3 Cl, Ti(CH 2 CMe 3 ) 3 Cl, Ti(CH 2 SiMe 3 ) 3 Cl, Ti(CH 2 Ph) 2 Cl 2 , Ti(CH 2 CMe 3 ) 2 Cl 2 , Ti(CH 2 SiMe 3 ) 2 Cl 2 , Ti(NMe 2 ) 4 , Ti(NEt 2 ) 4 , Ti(O-isopropyl) 4 , and Ti(N(SiMe 3 ) 2 ) 2 Cl 2 ; HfCl 4 , Hf(CH 2 Ph) 4 , Hf(CH 2 CMe 3 ) 4 , Hf(CH 2 SiMe 3 ) 4 , Hf(CH 2 Ph) 3 Cl, Hf(CH 2 Ph) 3 Cl
  • Lewis base adducts of these examples are also suitable as metal precursors, for example, ethers, amines, thioethers, phosphines and the like are suitable as Lewis bases.
  • Specific examples include HfCl 4 (THF) 2 , HfCl 4 (SMe 2 ) 2 and Hf(CH 2 Ph) 2 Cl 2 (OEt 2 ).
  • Activated metal precursors may be ionic or zwitterionic compounds, such as (M(CH 2 Ph) 3 + )(B(C 6 F 5 ) 4 ⁇ ) or (M(CH 2 Ph) 3 + )(PhCH 2 B(C 6 F 5 ) 3 ⁇ ) where M is defined above (and more specifically Hf or Zr).
  • Activated metal precursors or such ionic compounds can be prepared in the manner shown in Pellecchia et al., Organometallics , 1994, 13, 298-302; Pellecchia et al., J. Am. Chem. Soc ., 1993, 115, 1160-1162; Pellecchia et al., Organometallics , 1993, 13, 3773-3775 and Bochmann et al., Organometallics , 1993, 12, 633-640, each of which is incorporated herein by reference.
  • the ligand to metal precursor compound ratio is typically in the range of about 0.01:1 to about 100:1, more specifically in the range of about 0.1:1 to about 10:1 and even more specifically about 1:1.
  • This invention in part, relates to new metal-ligand complexes.
  • the ligand is mixed with a suitable metal precursor (and optionally other components, such as activators) prior to or simultaneously with allowing the mixture to be contacted with the reactants (e.g., monomers).
  • a metal-ligand complex may be formed, which may be a catalyst or may need to be activated to be a catalyst.
  • the metal-ligand complexes of this invention can in general be characterized in overlapping or alterative descriptions.
  • the metal-ligand complexes have dianionic, chelating ligands that may occupy up to four coordination sites of the metal atom.
  • the metal-ligand complexes can also be described as having dianionic ligands that form two seven-member metallocycles with the metal atom (counting the metal atom as one member of the seven member ring).
  • the metal-ligand complexes can be described as having dianionic, chelating ligands that use oxygen and/or sulfur as binding atoms to the metal atom.
  • the metal-ligand complexes can be described as having non-metallocene ligands that can coordinate in an approximate C 2 symmetric complex with the metal atom.
  • approximate C 2 symmetry it is meant that coordination of the ligand with the metal may still be considered so that the ligand parts occupy four approximately C 2 symmetric quadrants around the metal center extending towards the ligands L and approximate means that true symmetry may not exist due to several factors that effect symmetry, including, for example, the effect of the bridge.
  • the bulky R 2 and/or R 12 group the ligand may be approximately C 2 symmetrically arranged around the metal center.
  • FIGS. 1 a and 1 b demonstrate what is meant herein by approximate C 2 symmetry. Also, this approximate symmetry can be determined by proton NMR.
  • the metal-ligand complexes of this invention can be characterized by the general formula: (4,2,O,S)ML n ′ (VI) where (4,2,O,S) is a dianionic ligand having at least 4 atoms that are each independently oxygen or sulfur and chelating to the metal M at 4 coordination sites through oxygen and/or sulfur atoms with two of the bonds between the oxygen or sulfur atoms and the metal being covelent in nature and two of the bonds being dative in nature (i.e., oxygen or sulfur atoms acting as Lewis bases and the metal center acting as a Lewis acid); M is a metal selected from the group consisting of groups 3-6 and Lanthanide elements of the Periodic Table of Elements, more specifically, from group 4 (Hf, Zr and Ti); L is independently selected from the group consisting of halide (F, Cl, Br, I), optionally substituted alkyl, alkenyl, alkynyl, heteroalkyl, heteroalkenyl, heteroalkynyl
  • the metal-ligand complexes of this invention are those comprising two seven-member metallocycles formed with bonds from the metal atom to at least 2 heteroatoms (e.g., O, S, N, P, Se and the like).
  • these metal-ligand complexes comprise two seven-member metallocycles and even more specifically, there are at least two seven-member metallocycles that are joined together by at least one bridging group.
  • two, bridged seven-member metallocycles form a symmetrical complex.
  • the metal-ligand complex below is one embodiment of this invention: where the complex includes two metallocycles bound by a single bridging group.
  • the metal-ligand complexes of this invention may be characterized by the general formulas: wherein each of AR, M, L, B, and n′, are as defined above; and the dotted lines indicate possible binding to the metal atom, provided that at least two of the dotted lines are covalent bonds.
  • X, X′, X 4 , X 5 , Y 2 and Y 3 are derived from the definitions detailed above in that at least two hydrogen atoms are removed from X, X′, X′′, X′′′, Y and Y′, in a manner known to those of skill in the art, to form the at least two covalent bonds between the X and/or Y moieties and the metal.
  • X and X′ and Y 2 and Y 3 are the same or different and are independently selected from the group consisting of oxygen, sulfur, —NR 30 —, and —PR 30 —, where R 30 is selected from the group consisting of hydride, halide, and optionally substituted hydrocarbyl, heteroatom-containing hydrocarbyl, silyl, boryl, alkoxy, aryloxy and combinations thereof.
  • Y 2 and Y 3 are the same or different and are independently selected from the group consisting of optionally substituted amino, phosphino, hydroxy, alkoxy, aryloxy, thioxy, alkylthio and arylthio.
  • X 4 and X 5 are the same or different and are independently selected from the group consisting of optionally substituted amino, phosphino, hydroxy, alkoxy, aryloxy, thioxy, alkylthio and arylthio, provided that when the bond to the metal is covalent
  • X 4 and X 5 are independently selected from the group consisting of oxygen, sulfur, —NR 30 —, and —PR 30 —.
  • L n ′ indicates that the metal M is bonded to a number n′ groups of L, as defined above.
  • the metal-ligand complexes of this invention may be characterized by the general formula: wherein each of R 1 , R 2 , R 3 , R 4 , R 5 , R 6 , R 7 , R 8 , R 9 , R 10 , R 11 , R 12 , R 13 , R 14 , R 15 , R 16 , R 17 , R 18 , R 19 , R 20 , M, L, n′, B, X, X′, Y 2 and Y 3 are as defined above and as further explained in connection which structures (VII) and (VIII).
  • the dotted lines indicate possible binding to the metal atom, provided that at least two of the dotted lines are covalent bonds.
  • the metal-ligand complexes of this invention may be characterized by the general formula: wherein R 2 , R 3 , R 4 , R 5 , R 6 , R 7 , R 8 , R 9 , R 10 , R 11 , R 12 , R 13 , R 14 , R 15 , R 16 , R 17 , R 18 , R 19 , M, L, n′, B, X, X′, Y 2 and Y 3 are as defined above are as defined above and as further explained in connection which structures (VII) and (VIII).
  • the dotted lines indicate possible binding to the metal atom, provided that at least two of the dotted lines are covalent bonds.
  • the metal-ligand complexes of this invention may be characterized by the general formula: wherein R 2 , R 3 , R 4 , R 5 , R 6 , R 7 , R 8 , R 9 , M, L, n′, B, X, X′, and Y 2 are as defined above are as defined above and as further explained in connection which structures (VII) and (VIII).
  • the dotted lines indicate possible binding to the metal atom, provided that at least two of the dotted lines are covalent bonds.
  • the metal-ligand complex may also have approximate C 2 symmetry that may provide control of tacticity in the polymerization of propylene to isotactic polypropylene, when combined with appropriate activator(s).
  • metal-ligand complexes specifics for the substituents on the ligands for production of the particular polymers discussed above (e.g., isotactic polypropylene) apply to the metal-ligand complexes.
  • Lewis base adducts of the metal-ligand complexes in the above formulas are also suitable, for example, ethers, amines, thioethers, phosphines and the like are suitable as Lewis bases.
  • the metal-ligand complexes can be formed by techniques known to those of skill in the art, such as combinations of metal precursors and ligands under conditions to afford complexation.
  • the complexes of this invention can be prepared according to the general scheme shown below:
  • a ligand according to formula (IV) is combined with the metal precursor under conditions to cause the removal of at least 2 leaving group ligands L, which are shown in the scheme as combining with a hydrogen (H).
  • Other schemes where the leaving group ligand combines with other moieties (e.g., Li) employing other known routes for complexation may be used, including for example, reactions where the ligand L reacts with other moieties (e.g., where the alkali metal salt of the ligand is used and the complexation reaction proceeds by salt elimation).
  • FIGS. 1 a and 1 b The x-ray crystal structure of molecule C5 is shown in FIGS. 1 a and 1 b.
  • the ligands, complexes or catalysts may be supported on organic or inorganic supports. Suitable supports include silicas, aluminas, clays, zeolites, magnesium chloride, polystyrenes, substituted polystyrenes and the like. Polymeric supports may be cross-linked or not. Similarly, the ligands, complexes or catalysts may be supported on similar supports known to those of skill in the art. See for example, Hlatky, Chem. Rev . 2000, 100, 1347-1376 and Fink et al., Chem. Rev . 2000, 100, 1377-1390, both of which are incorporated herein by reference. In addition, the catalysts of this invention may be combined with other catalysts in a single reactor and/or employed in a series of reactors (parallel or serial) in order to form blends of polymer products.
  • the metal-ligand complexes and compositions are active catalysts typically in combination with a suitable activator, combination of activators, activating technique or activating package, although some of the ligand-metal complexes may be active without an activator or activating technique.
  • the activator(s) may comprise alumoxanes, Lewis acids, Bronsted acids, compatible non-interfering activators and combinations of the foregoing.
  • Suitable ion forming compounds useful as an activator in one embodiment of the present invention comprise a cation that is a Bronsted acid capable of donating a proton, and an inert, compatible, non-interfering, anion, A ⁇ .
  • Preferred anions are those containing a single coordination complex comprising a charge-bearing metal or metalloid core.
  • said anion should be sufficiently labile to be displaced by olefinic, diolefinic and unsaturated compounds or other neutral Lewis bases such as ethers or nitriles.
  • Suitable metals include, but are not limited to, aluminum, gold and platinum.
  • Suitable metalloids include, but are not limited to, boron, phosphorus, and silicon.
  • Compounds containing anions that comprise coordination complexes containing a single metal or metalloid atom are, of course, well known and many, particularly such compounds containing a single boron atom in the anion portion are available commercially.
  • activators may be represented by the following general formula: (L*—H) d + (A d ⁇ ) wherein L* is a neutral Lewis base; (L*—H) + is a Bronsted acid; A d ⁇ is a non-interfering, compatible anion having a charge of d ⁇ , and d is an integer from 1 to 3.
  • d is one, i.e., the counter ion has a single negative charge and corresponds to the formula A ⁇ .
  • Activators comprising boron or aluminum which are particularly useful in the preparation of catalysts of this invention may be represented by the following general formula: (L*—H) + (JQ 4 ) ⁇ wherein: L* is as previously defined; J is boron or aluminum; and Q is a fluorinated C 1-20 hydrocarbyl group. Most specifically, Q is independently selected from the group selected from the group consisting of fluorinated aryl group, especially, a pentafluorophenyl group (i.e., a C 6 F 5 group) or a 3,5-bis(CF 3 ) 2 C 6 H 3 group.
  • Specific (L*—H) + cations are N,N-dimethylanilinium and HNMe(C 18 H 37 ) + .
  • Specified anions are tetrakis(3,5-bis(trifluoromethyl)phenyl)borate and tetrakis(pentafluorophenyl)borate.
  • the specific activator is PhNMe 2 H + B(C 6 F 5 ) 4 ⁇ .
  • Suitable ion forming activators comprise a salt of a cationic oxidizing agent and a non-interfering, compatible anion represented by the formula: (Ox e+ ) d (A d ⁇ ) e wherein: Ox e+ is a cationic oxidizing agent having a charge of e+; e is an integer from 1 to 3; and A d ⁇ , and d are as previously defined.
  • cationic oxidizing agents include: ferrocenium, hydrocarbyl-substituted ferrocenium, Ag + , or Pb +2 .
  • Specific embodiments of A d ⁇ are those anions previously defined with respect to the Bronsted acid containing activating cocatalysts, especially tetrakis(pentafluorophenyl)borate.
  • Another suitable ion forming, activating cocatalyst comprises a compound that is a salt of a carbenium ion or silyl cation and a non-interfering, compatible anion represented by the formula: ⁇ circle around (c) ⁇ + A ⁇ wherein: ⁇ circle around (c) ⁇ + is a C 1-100 carbenium ion or silyl cation; and A ⁇ is as previously defined.
  • a preferred carbenium ion is the trityl cation, i.e. triphenylcarbenium.
  • the silyl cation may be characterized by the formula Z 4 Z 5 Z 6 Si + cation, where each of Z 4 , Z 5 , and Z 6 is independently selected from the group consisting of hydride, halide, and optionally substituted alkyl, alkenyl, alkynyl, heteroalkyl, heteroalkenyl, heteroalkynyl, aryl, heteroaryl, alkoxyl, aryloxyl, silyl, boryl, phosphino, amino, thioxy, alkylthio, arylthio, and combinations thereof.
  • a specified activator is Ph 3 C + B(C 6 F 5 ) 4 ⁇ .
  • Suitable activating cocatalysts comprise a compound that is a salt, which is represented by the formula (A* +a ) b (Z*J* j ) ⁇ c d wherein A* is a cation of charge +a; Z* is an anion group of from 1 to 50, specifically 1 to 30 atoms, not counting hydrogen atoms, further containing two or more Lewis base sites; J* independently each occurrence is a Lewis acid coordinated to at least one Lewis base site of Z*, and optionally two or more such J* groups may be joined together in a moiety having multiple Lewis acidic functionality; j is a number form 2 to 12; and a, b, c, and d are integers from 1 to 3, with the proviso that a ⁇ b is equal to c ⁇ d.
  • the anion portion of these activating cocatalysts may be characterized by the formula ((C 6 F 5 ) 3 M′′′′—LN—M′′′′(C 6 F 5 ) 3 ) ⁇ where M′′′′ is boron or aluminum and LN is a linking group, which is specifically selected from the group consisting of cyanide, azide, dicyanamide and imidazolide.
  • the cation portion is specifically a quaternary amine. See, e.g., LaPointe, et al., J. Am. Chem. Soc . 2000, 122, 9560-9561, which is incorporated herein by reference.
  • suitable activators include Lewis acids, such as those selected from the group consisting of tris(aryl)boranes, tris(substituted aryl)boranes, tris(aryl)alanes, tris(substituted aryl)alanes, including activators such as tris(pentafluorophenyl)borane.
  • Lewis acids such as those selected from the group consisting of tris(aryl)boranes, tris(substituted aryl)boranes, tris(aryl)alanes, tris(substituted aryl)alanes, including activators such as tris(pentafluorophenyl)borane.
  • Other useful ion forming Lewis acids include those having two or more Lewis acidic sites, such as those described in WO 99/06413 or Piers, et al.
  • activators or compounds useful in a polymerization reaction may be used. These compounds may be activators in some contexts, but may also serve other functions in the polymerization system, such as alkylating a metal center or scavenging impurities. These compounds are within the general definition of “activator,” but are not considered herein to be ion-forming activators.
  • G 13 is selected from the group consisting of B, Al, Ga, In and combinations thereof, p is 0, 1 or 2
  • each R 50 is independently selected from the group consisting of hydride, halide, and optionally substituted alkyl, alkenyl, alkynyl, heteroalkyl, heteroalkenyl, heteroalkynyl, aryl, heteroaryl, and combinations thereof
  • each D is independently selected from the group consisting of halide, hydride, alkoxy, aryloxy, amino, thioxy, alkylthio, arylthio, phosphino and combinations thereof.
  • the group 13 activator is an oligomeric or polymeric alumoxane compound, such as methylalumoxane and the known modifications thereof.
  • a divalent metal reagent may be used that is defined by the general formula M′R 50 2 ⁇ p′ D p′ and p′ is 0 or 1 in this embodiment and R 50 and D are as defined above.
  • M′ is the metal and is selected from the group consisting of Mg, Ca, Sr, Ba, Zn, Cd and combinations thereof.
  • an alkali metal reagent may be used that is defined by the general formula M′′R 50 and in this embodiment R 50 is as defined above.
  • M′′ is the alkali metal and is selected from the group consisting of Li, Na, K, Rb, Cs and combinations thereof.
  • hydrogen and/or silanes may be used in the catalytic composition or added to the polymerization system.
  • Silanes may be characterized by the formula SiR 50 4 ⁇ q D q where R 50 is defined as above, q is 1, 2, 3 or 4 and D is as defined above, with the proviso that there is at least one D that is a hydride.
  • the molar ratio of metal:activator (whether a composition or complex is employed as a catalyst) employed specifically ranges from 1:10,000 to 100:1, more specifically from 1:5000 to 10:1, most specifically from 1:10 to 1:1.
  • mixtures of the above compounds are used, particularly a combination of a group 13 reagent and an ion-forming activator.
  • the molar ratio of group 13 reagent to ion-forming activator is specifically from 1:10,000 to 1000:1, more specifically from 1:5000 to 100:1, most specifically from 1:100 to 100:1.
  • the ion forming activators are combined with a group 13 reagent.
  • Another embodiment is a combination of the above compounds having about 1 equivalent of N,N-dimethylanilinium tetrakis(pentafluorophenyl) borate, and 5-30 equivalents of a Group 13 reagent.
  • the ligand will be mixed with a suitable metal precursor compound prior to or simultaneous with allowing the mixture to be contacted to the reactants.
  • a metal-ligand complex may be formed, which may be a catalyst.
  • compositions, complexes and/or catalysts of this invention are particularly effective at polymerizing ⁇ -olefins (such as propylene, 1-butene, 1-pentene, 1-hexene, 1-heptene, 1-octene, and styrene), copolymerizing ethylene with ⁇ -olefins (such as propylene, 1-butene, 1-pentene, 1-hexene, 1-heptene, 1-octene, and styrene), and copolymerizing ethylene with 1,1-disubstituted olefins (such as isobutylene).
  • ⁇ -olefins such as propylene, 1-butene, 1-pentene, 1-hexene, 1-heptene, 1-octene, and styrene
  • ⁇ -olefins such as propylene, 1-butene, 1-pentene, 1-hexene, 1-heptene,
  • compositions might also polymerize monomers that have polar functionalities in homopolymerizations or copolymerizations and/or homopolymerize 1,1- and 1,2-disubstituted olefins.
  • diolefins in combination with ethylene and/or ⁇ -olefins or 1,1- and 1,2-disubstituted olefins may be copolymerized.
  • monomers useful herein may be olefinically or unsaturated monomers having from 2 to 20 carbon atoms either alone or in combination.
  • monomers may include olefins, diolefins and unsaturated monomers including ethylene and C 3 to C 20 ⁇ -olefins such as propylene, 1-butene, 1-hexene, 1-octene, 4-methyl-1-pentene, 1-norbornene, styrene and mixtures thereof, additionally, 1,1-disubstituted olefins, such as isobutylene, 2-methyl-1-butene, 2-methyl-1-pentene, 2-ethyl-1-pentene, 2-methyl-1-hexene, 3-trimethylsilyl-2-methyl-1-propene, ⁇ -methyl-styrene, either alone or with other monomers such as ethylene or C 3 to C 20 ⁇ -olefins and/or diolefins; additionally 1,2-
  • the ⁇ -olefins listed above may be polymerized in a stereospecific manner e.g. to generate isotactic or syndiotactic or hemiisotactic polypropylene. Additionally the ⁇ -olefins may be polymerized to produce a polymer with differing tacticity sequences within the polymer chain, such as polypropylene containing atactic and isotactic sequences within the same polymer chain. These definitions are intended to include cyclic olefins.
  • Diolefins generally comprise 1,3-dienes such as (butadiene), substituted 1,3-dienes (such as isoprene) and other substituted 1,3-dienes, with the term substituted referring to the same types of substituents referred to above in the definition section.
  • Diolefins also comprises 1,5-dienes and other non-conjugated dienes.
  • the styrene monomers may be unsubstituted or substituted at one or more positions on the aryl ring.
  • the use of diolefins in this invention is typically in conjunction with another monomer that is not a diolefin. In some embodiments, acetylenically unsaturated monomers may be employed.
  • the catalysts of the present invention are particularly active for certain monomers, particularly ⁇ -olefins.
  • the catalysts of the present invention may provide higher comonomer incorporation for copolymers of ethylene and co-monomers having three or more carbon atoms than is currently known from other catalysts. It has been found that particular catalysts of the present invention co-polymerize ethylene and styrene (or substituted styrenes), forming ethylene-styrene copolymers.
  • Polymers that can be prepared according to the present invention include ethylene copolymers with at least one C 3 -C 20 ⁇ -olefin, particularly propylene, 1-butene, 1-hexene, 4-methyl-1-pentene and 1-octene.
  • the copolymers of ethylene with at least one C 3 -C 20 ⁇ -olefin comprise from about 0.1 mol. % ⁇ -olefin to about 50 mol. % ⁇ -olefin, more specifically from about 0.2 mol. % ⁇ -olefin to about 50 mol. % ⁇ -olefin and still more specifically from about 2 mol. % ⁇ -olefin to about 30 mol. % higher olefin.
  • copolymers include those of ethylene and a comonomer selected from the group consisting of propylene, 1-butene, 1-hexene, and 1-octene comprise from about 0.2 to about 30 mol. % comonomer, more specifically from about 1 to about 20 mol. % comonomer, even more specifically from about 2 to about 15 mol. % comonomer and most specifically from about 5 to about 12 mol. % comonomer.
  • Novel polymers, copolymers or interpolymers may be formed having unique physical and/or melt flow properties.
  • Such novel polymers can be employed alone or with other polymers in a blend to form products that may be molded, cast, extruded or spun.
  • End uses for the polymers made with the catalysts of this invention include films for packaging, trash bags, bottles, containers, foams, coatings, insulating devices and household items. Also, such functionalized polymers are useful as solid supports for organometallic or chemical synthesis processes.
  • the ⁇ -olefins listed above may be polymerized in a stereoselective manner e.g. to generate isotactic or syndiotactic or hemiisotactic poly- ⁇ -olefins.
  • 1-butene may be polymerized into isotactic poly-1-butene.
  • the ⁇ -olefins may be polymerized to produce a polymer with differing tacticity sequences within the polymer chain, such as polypropylene containing atactic and isotactic sequences within the same polymer chain.
  • the stereoregularity may be interrupted by stereoerrors, in particular isolated stereoerrors, which is an indication of enantiomorphic side control.
  • regioerrors might be present in the isotactic polypropylene polymer as it is described in the literature (see, e.g., Resconi et al., “Selectivity in Propene Polymerization with Metallocene Catalysts,” Chem. Rev. 2000, 100, 1253-1345).
  • isotactic polypropylene can be produced having a narrow polydispersity (e.g., less than about 3.0 and more specifically less than 2.5) combined with a high molecular weight (e.g., greater than about 50,000, more specifically greater than about 100,000 and even more specifically greater than about 150,000) in a solution polymerization process at a temperature of greater than about 100° C., more specifically greater than 110° C. and even more specifically greater than 130° C.
  • isotactic polypropylene produced by certain embodiments of this invention can be prepared with few or no detectible using 13 C NMR regio-errors (also known as regio-irrgularities). This is shown in FIG. 2 where the regio-errors are not detectible in certain isotactic polypropylene polymers prepared as discussed in the examples, using 13 C NMR methods as described in Rescnoi et al. cited above. It is intended that the 13 C NMR used herein are typical for polymer characterization.
  • the isotactic polypropylene polymers formed from these catalysts in a solution polymerization process can be produced at a higher temperature than has been described before, such as at a temperature of greater than about 100° C., more specifically greater than 110° C. and even more specifically greater than 130° C.
  • the polymerization conditions are described herein, producing isotactic polypropylene with a crystallinity index of between about 0.35 and about 0.95, more specifically between about 0.65 and 0.95 and in some embodiments specifically above about 0.8, under the polymerization conditions employed.
  • the crystallinity index is determined using FTIR as is known to those of skill in the art and calibrated based on a relative scale.
  • the crystallinity index value can be determined using commercially available FTIR equipment (such as a Bruker Equinox 55 with an IR Scope II in reflection mode using Pike MappIR software).
  • the crystallinity index is obtained from the ratio of band heights at 995 cm ⁇ 1 and 972 cm ⁇ 1 .
  • Atactic polypropylene has a ratio of band heights or crystallinity index of 0.2. Greater than 98% isotactic polypropylene has a crystallinity index ratio of greater than 0.95.
  • the amount of error in crystallinity index measurements is ⁇ 0.05.
  • Polymer blends of various compositions show a linear relationship between % isotacticity and crystallinity index. See, for example, J. P.
  • isotacticity can also be represented by percent pentads (% mmmm) as determined by 13 C NMR spectroscopy.
  • Proton decoupled 13 C NMR spectroscopy can be performed using commercially available equipment (such as a Bruker 300 MHz at 100° C. probe temperature) to determine the degree of tacticity as % mmmm pentads (for assignment of 13 C signals see the review Brintzinger H. H. et al., Angew. Chem. Int. Ed. Eng . 1995, 34, 1143, which is incorporated herein by reference; and Resconi, Chem. Rev . 2000, 100, 1253-1345 and Gibson, et al., Chem Rev .
  • a 15-30 mg polymer sample is dissolved in a 1:1 mixture of C 2 D 2 Cl 4 and C 2 Cl 4 by heating the sample to ca. 100° C.
  • the % mmmm is determined by the ratio of peak integral from 23.5 to 21.5 ppm and peak integral 23.5 to 19 ppm (in the absence of significant chain end regio-irregularity signals in this region).
  • Proton decoupled 13 C NMR spectroscopy can be also performed to determine the frequency of and nature of stereoerrors and regioerrors.
  • the melting point of the crystalline polypropylene is generally in the range of from about 115° C. to about 165° C., more specifically between about 120° C. and 155° C., and in some embodiments specifically above about 135° C. Melting points are determined by differential scanning calorimetry, as is known in the art (see also the example section, herein).
  • Novel polymers, copolymers or interpolymers may be formed having unique physical and/or melt flow properties.
  • Polymers that can be prepared according to the present invention include propylene copolymers with at least one C 4 -C 20 ⁇ -olefin, particularly 1-butene, 1-hexene, 4-methyl-1-pentene and 1-octene.
  • the copolymers of propylene with at least one C 4 -C 20 ⁇ -olefin comprise from about 0.1 wt. % higher olefin to about 60 wt. % higher olefin, more specifically from about 0.2 wt. % higher olefin to about 50 wt. % higher olefin and still more specifically from about 2 wt.
  • crystalline copolymers include those of propylene and a comonomer selected from the group consisting of ethylene, 1-butene, 1-hexene, and 1-octene comprise from about 0.2 to about 30 wt. % comonomer, more specifically from about 1 to about 20 wt. % comonomer, even more specifically from about 2 to about 15 wt. % comonomer and most specifically from about 5 to about 12 wt. % comonomer.
  • novel polymers such as isotactic polypropylene
  • other natural or synthetic polymers can be polyethylene (including linear low density polyethylene, low density polyethylene, high density polyethylene, etc.), atactic polypropylene, nylon, EPDM, ethylene-propylene elastomer copolymers, polystyrene (including syndiotactic polystryene), ethylene-styrene copolymers and terpolymers of ethylene-styrene and other C 3 -C 20 olefins (such as propylene).
  • polyethylene including linear low density polyethylene, low density polyethylene, high density polyethylene, etc.
  • atactic polypropylene nylon
  • EPDM ethylene-propylene elastomer copolymers
  • polystyrene including syndiotactic polystryene
  • ethylene-styrene copolymers and terpolymers of ethylene-styrene and other C 3 -C 20
  • Melt flow rate (MRF) for polypropylene and copolymer of propylene and one or more C 4 -C 20 ⁇ -olefins is measured according to ASTM D-1238, condition L (2.16 kg, 230° C.). In some embodiments of this invention, the MFR is in the range of 0.005-1,000, more specifically 0.01-500 and even more specifically 0.1-100. Flex modulus for polypropylene and copolymer of propylene and one or more C 4 -C 20 ⁇ -olefins is measured according to ASTM D-790.
  • the flex modulus ranges from 20,000-400,000 psi, more specifically from 20,000-300,000 psi and even more specifically from 100,000-200,000 psi.
  • Notch izod impact for polypropylene and copolymer of propylene and one or more C 4 -C 20 ⁇ -olefins is measured according to ASTM D-256A.
  • the notch izod impact ranges from 0.1 to no break in ft-lbs/in.
  • novel polypropylene and copolymer of propylene and one or more C 4 -C 20 ⁇ -olefins disclosed in the present invention are useful for a wide variety of applications, including films (such as blown and cast film, clarity film and multi-layer films), thermoforming (such as cups, plates, trays and containers), injection moulding, blow-moulding, foams (such as structural foams), pipe (such as potable water pipe and high pressure pipe), automotive parts, and other applications that will be evident to those of skill in the art.
  • films such as blown and cast film, clarity film and multi-layer films
  • thermoforming such as cups, plates, trays and containers
  • injection moulding blow-moulding
  • foams such as structural foams
  • pipe such as potable water pipe and high pressure pipe
  • automotive parts and other applications that will be evident to those of skill in the art.
  • Melt strength (measured in cN) and melt drawability (measured in mm/s) tests are conducted by pulling (“taking-up”) strands of the molten polymers or blends at constant acceleration until breakage occurs.
  • An experimental set-up comprises a capillary rheometer and a Rheotens apparatus as a take-up device. The molten strands are drawn uniaxially to a set of accelerating nips located 100 mm below the die. The force required to uniaxially extend the strands is recorded as a function of the take-up velocity or the nip rolls.
  • melt strength In the case of polymer melts exhibiting draw resonance (indicated by the onset of a periodic oscillation of increasing amplitude in the measured force profile), the maximum force and wheel velocity before the onset of draw resonance are taken as the melt strength and melt drawability, respectively. In the absence of draw resonance, the maximum force attained during testing is defined as the melt strength and the velocity at which breakage occurs is defined as the melt drawability.
  • Mass flow rate 1.35 grams/min Temperature 190° C. Equilibration time at 190° C. 10 minutes Die 20:1 (with entrance angle of approximately 45 degrees) Capillary length 41.9 mm Capillary diameter 2.1 mm Piston diameter 9.54 mm Piston velocity 0.423 mm/s Shear rate 33.0 s ⁇ 1 Draw-down distance (die exit to take-up 100 mm sheels) Cooling conditions Ambient air Acceleration 2.4 mm/s 2
  • the novel polymers are useful to produce foams having improved properties.
  • the MFR is typically in the range of 0.1-10, more specifically in the range of 0.3-3 and most specifically in the range of 0.5-2.
  • the melt strength is typically greater than 5 cN, more specifically greater than 9 cN and most specifically greater than 12 cN.
  • the drawability is typically greater than 15 mm/sec, more specifically greater than 25 mm/sec and most specifically greater than 35 mm/sec.
  • the novel polymers disclosed herein are useful for a wide variety of applications where certain optical properties are beneficial. Gloss is measured according to ASTM D-1746. Haze is measured according to ASTM D-1003 and clarity is measured according to ASTM D-2457.
  • the novel polymers disclosed herein in some aspects are films having haze of less than 10%. In addition films having clarity of greater than 91% may be beneficially obtained.
  • Polymerization is carried out under polymerization conditions, including temperatures of from ⁇ 100° C. to 300° C. and pressures from atmospheric to 3000 atmospheres.
  • Suspension, solution, slurry, gas phase or high-pressure polymerization processes may be employed with the catalysts and compounds of this invention. Such processes can be run in a batch, semi-batch or continuous mode. Examples of such processes are well known in the art.
  • a support for the catalyst may be employed, which may be inorganic (such as alumina, magnesium chloride or silica) or organic (such as a polymer or cross-linked polymer). Methods for the preparation of supported catalysts are known in the art. Slurry, suspension, gas phase and high-pressure processes as known to those skilled in the art may also be used with supported catalysts of the invention.
  • additives that are useful in a polymerization reaction may be employed, such as scavengers, promoters, modifiers and/or chain transfer agents, such as hydrogen, aluminum alkyls and/or silanes.
  • catalytic performance can be determined a number of different ways, as those of skill in the art will appreciate. Catalytic performance can be determined by the yield of polymer obtained per mole of metal complex, which in some contexts may be considered to be activity. The examples provide data for these comparisons.
  • catalyst polymerization performance is co-monomer incorporation.
  • many ethylene copolymers are prepared using ethylene and at least one other monomer. These copolymers or higher order polymers in some applications require higher amounts of additional co-monomer(s) than have been practical with known catalysts. Since ethylene tends to be the most reactive monomer, obtaining higher co-monomer incorporations is a benefit that is examined for polymerization catalysts.
  • Two useful co-monomers are 1-octene and styrene. This invention offers the possibility of higher incorporation of co-monomers such as 1-octene and styrene.
  • a solution process is specified for certain benefits, with the solution process being run at a temperature above 90° C., more specifically at a temperature above 100° C., further more specifically at a temperature above 110° C. and even further more specifically at a temperature above 130° C.
  • Suitable solvents for polymerization are non-coordinating, inert liquids.
  • Examples include straight and branched-chain hydrocarbons such as isobutane, butane, pentane, isopentane, hexane, isohexane, heptane, octane, Isopar-E® and mixtures thereof; cyclic and alicyclic hydrocarbons such as cyclohexane, cycloheptane, methylcyclohexane, methylcycloheptane, and mixtures thereof; perhalogenated hydrocarbons such as perfluorinated C 4-10 alkanes, chlorobenzene, and aromatic and alkyl substituted aromatic compounds such as benzene, toluene, mesitylene, and xylene.
  • straight and branched-chain hydrocarbons such as isobutane, butane, pentane, isopentane, hexane, isohexane, heptane, octane, Isopar-E
  • Suitable solvents also include liquid olefins which may act as monomers or comonomers including ethylene, propylene, 1-butene, butadiene, cyclopentene, 1-hexene, 1-pentene, 3-methyl-1-pentene, 4-methyl-1-pentene, 1,4-hexadiene, 1-octene, 1-decene, isobutylene, styrene, divinylbenzene, allylbenzene, and vinyltoluene (including all isomers alone or in admixture). Mixtures of the foregoing are also suitable.
  • liquid olefins which may act as monomers or comonomers including ethylene, propylene, 1-butene, butadiene, cyclopentene, 1-hexene, 1-pentene, 3-methyl-1-pentene, 4-methyl-1-pentene, 1,4-hexadiene, 1-octene, 1-decene, isobutylene
  • a solution process is specified for crystalline polypropylene production.
  • the solution process to prepare isotactic polypropylene comprises adding a catalyst and propylene monomer to a reactor and subjecting the contents to polymerization conditions.
  • the ligands, metal-ligand complexes and compositions of this invention can be prepared and tested for catalytic activity in one or more of the above reactions in a combinatorial fashion.
  • Combinatorial chemistry generally involves the parallel or rapid serial synthesis and/or screening or characterization of compounds and compositions of matter.
  • U.S. Pat. Nos. 5,985,356, 6,030,917 and WO 98/03521, all of which are incorporated herein by reference, generally disclose combinatorial methods.
  • the ligands, metal-ligand complexes or compositions may be prepared and/or tested in rapid serial and/or parallel fashion, e.g., in an array format.
  • ligands, metal-ligand complexes or compositions may be take the form of an array comprising a plurality of compounds wherein each compound can be characterized by any of the above general formulas (i.e., I, II, III, etc.).
  • An array of ligands may be synthesized using the procedures outlined previously.
  • the array may also be of metal precursor compounds, the metal-ligand complexes or compositions characterized by the previously described formulae and/or description.
  • each member of the array will have differences so that, for example, a ligand or activator or metal precursor or R group in a first region of the array may be different than the ligand or activator or metal precursor or R group in a second region of the array. Other variables may also differ from region to region in the array.
  • each of the plurality of compositions or complexes has a different composition or stoichiometry, and typically each composition or complex is at a selected region on a substrate such that each compound is isolated from the other compositions or complexes.
  • This isolation can take many forms, typically depending on the substrate used. If a flat substrate is used, there may simply be sufficient space between regions so that there cannot be interdiffusion between compositions or complexes.
  • the substrate can be a microtiter or similar plate having wells so that each composition or complex is in a region separated from other compounds in other regions by a physical barrier.
  • the array may also comprise a parallel reactor or testing chamber.
  • the array typically comprises at least 8 compounds, complexes or compositions each having a different chemical formula, meaning that there must be at least one different atom or bond differentiating the members in the array or different ratios of the components referred to herein (with components referring to ligands, metal precursors, activators, group 13 reagents, solvents, monomers, supports, etc.).
  • the catalytic performance of the compounds, complexes or compositions of this invention can be tested in a combinatorial or high throughput fashion.
  • Polymerizations can also be performed in a combinatorial fashion, see, e.g., U.S. Pat. Nos. 6,306,658, 6,508,984 and WO 01/98371, each of which is herein incorporated by reference.
  • the system was operated at a eluent flow rate of 1.5 mL/min and an oven temperature of 160° C. o-dichlorobenzene was used as the eluent.
  • the polymer samples were dissolved 1,2,4-trichlorobenzene at a concentration of about 1 mg/mL. Between 40 ⁇ L and 200 ⁇ L of a polymer solution were injected into the system. The concentration of the polymer in the eluent was monitored using an evaporative light scattering detector. All of the molecular weight results obtained are relative to linear polystyrene standards.
  • the ratio of 1-octene to ethylene incorporated in the ethylene-octene copolymer products was determined by Raman spectroscopy. All spectra were obtained using a Bruker Equinox 055 FRA 106/S FT-Raman Spectrometer (Raman back scattering) with a 4 min acquisition time, a laser power of 500 mW, and spectral resolution of 4 cm ⁇ 1 . Analysis was performed using OPUS NT software package by measuring the absorbance of the peaks at 2953, 2955, and 2957 cm ⁇ 1 (for the asymmetric CH 3 stretch) and the peak maximum between 2844 and 2854 cm ⁇ 1 (for the symmetric CH 2 stretch).
  • Crystallinity in polypropylene was determined by FTIR spectroscopy.
  • FTIR spectra of thin films deposited from solution onto gold coated Si wafers are acquired at 4 cm ⁇ 1 resolution and with 16 scans in reflection-absorption mode on a Bruker Equinox 55 FTIR spectrometer equipped with a Pike MappIR accessory.
  • the height ratio of two bands at 995 cm ⁇ 1 (C—H bending and CH 3 rocking mode from regular crystalline isotactic helices) and 972 cm ⁇ 1 (coupled C—C stretching and CH 3 rocking mode, independent of crystallinity) is determined as a measure of isotacticity (as known in the art, see, e.g., J. P.
  • the ratio of styrene to ethylene incorporated in the polymer products was determined using FTIR spectroscopy.
  • the IR spectra (16 scans at 4 cm ⁇ 1 resolution) analyzed by Partial Least Squares (PLS) analysis with PLSplus/IQ V3.04 for GRAMS/32 (Galactic Industries) software, using the following training set for calibration.
  • PLS Partial Least Squares
  • the analysis based on a training set consisting of 180 spectra of blends of ethylene-styrene copolymers with known styrene incorporation, and atactic homo-polystyrene.
  • the 16 known copolymers had between 1 and 47 mol % incorporated styrene.
  • the atactic homo-polystyrene content in the blends ranged from 0 to 90% of the total styrene content of the blend. Most blends are prepared from copolymers with up to 20 mol % incorporation. Multiple spectra per blend were included in the training set.
  • FTIR method for determining mol % total styrene in product FTIR was performed on a Bruker Equinox 55+IR Scope II in reflection mode using a Pike MappIR accessory with 16 scans. The ratio of total styrene to ethylene was obtained from the ratio of band heights at 4330 cm ⁇ 1 and 1602 cm ⁇ 1 . This method was calibrated using a set of ethylene-styrene copolymers with a range of known styrene content.
  • the total styrene content of the polymer products includes both the styrene incorporated in the ethylene-styrene copolymer and any background homopolystyrene (PS) in the product sample.
  • PS homopolystyrene
  • the homopolystyrene background level is typically less than 3.5 wt % (1 mol %).
  • DSC Differential Scanning Calorimetry
  • ligands in these examples are prepared according to the general schemes described above and shown below, where “building blocks” are first prepared and then coupled together.
  • Step 1 n-BuLi (22.5 mmol, from a 1.6 M solution in hexanes, 14 mL) was added slowly to a solution of the aryl bromide (21.44 mmol, 5 g) in THF (50 mL, anhydrous) at ⁇ 78° C. under an atmosphere of argon. After stirring for 30 min at that temperature, triisopropyl borate (25.7 mmol, 6 mL) was added slowly and the temperature was allowed to come to room temperature (30 min). After stirring for another 30 min, the solvent was removed and the crude boronic acid was used without further purification.
  • Step 2 A mixture of the protected 2-bromophenol (methyl ether, 3.38 g, 16.8 mmol), the boronic acid (22.5 mmol), Na 2 CO 3 (9 mL of a 2 M solution in water, 18 mmol) and dimethoxy ethane (100 mL) was degassed with argon. Pd(PPh 3 ) 3 (485 mg, 0.42 mmol, 2.5%) was added and the resulting mixture was stirred at 85° C. for 16 h under argon. Ethyl acetate (30 mL) was added and the mixture was dried over Na 2 SO 4 .
  • n-BuLi (4 mmol, from a 1.6 M solution in hexanes, 2.5 mL) was added slowly to a solution of the aryl bromide (3.72 mmol, 1 g) in THF (10 mL, anhydrous) at ⁇ 78° C. under an atmosphere of argon. After stirring for 10 min at that temperature, triisopropyl borate (4.3 mmol, 988 ⁇ L) was added slowly and the temperature was allowed to come to room temperature (30 min). After stirring for another 30 min, the solvent was removed and the crude aryl boronic acid was used without further purification.
  • n-BuLi (2.6 mmol, from a 1.6 M solution in hexanes) was added slowly to a solution of the benzyl ether protected 2-bromophenol (2.47 mmol) in THF (5 mL, anhydrous) at ⁇ 78° C. under an atmosphere of argon. After stirring for 10 min at that temperature, triisopropyl borate (645 ⁇ L, 2.8 mmol) was added slowly and the temperature was allowed to come to room temperature (30 min). After stirring for another 30 min, the solvent was removed and the crude boronic acid was used without further purification.
  • a pre-weighed glass vial insert and disposable stirring paddle were fitted to each reaction vessel of the reactor.
  • the reactor was then closed, 0.10 mL of a 0.02 M solution of group 13 reagents in toluene and 3.9 mL of toluene were injected into each pressure reaction vessel through a valve.
  • the identity of the group 13 reagent solution is given in Tables 1-3.
  • the temperature was then set to the appropriate setting (with specific temperatures for each polymerization being listed in Tables 1-3, below), and the stirring speed was set to 800 rpm, and the mixture was exposed to propylene at 100 psi pressure.
  • a propylene pressure of 100 psi in the pressure cell and the temperature setting were maintained, using computer control, until the end of the polymerization experiment.
  • Method A An appropriate amount of ligand solution (10 mM in toluene) was dispensed in a 1 mL glass vial at a scale of 0.4-0.75 mmol. To the 1 mL glass vial containing the ligand solution was added an equimolar amount of metal precursor solution (10 mM in toluene) to form the metal-ligand composition solution. The reaction mixture was heated to 70-80° C. for 1-2 hours. Method B: Similar to Method A except the reaction mixture was heated to 60° C. for 1-2 hours. Method C: Similar to Method A except the reaction mixture was heated to 80° C. for 1-2 hours.
  • Method D Similar to Method A except the concentration of ligand and metal precursor solutions were 5 mM. The reaction mixture was allowed to sit at room temperature for 35 min and than was heated to 70-80° C. for 10 min.
  • Method E Similar to Method B except the concentration of ligand and metal precursor solutions were 5 mM.
  • Method F Similar to Method A except the concentration of ligand solution was 5 mM and metal precursor solution was 10 mM. The reaction mixture was heated for 30 min to 50° C.
  • Method G Similar to Method A except the concentration of ligand solution was 15 mM and metal precursor solution was 10 mM. The reaction mixture was heated for 1 hour to 70° C.
  • Method H Similar to Method A except the concentration of ligand solution was 60 mM and metal precursor solution was 5 mM. The reaction mixture was heated for 45 min to 70° C.
  • Method I Similar to Method G except the concentration of ligand solution was 25 mM and metal precursor solution was 5 mM.
  • Method J Similar to Method H except the concentration of ligand solution was 12 mM and metal precursor solution was 5 mM.
  • the “activator solution” is a solution of N,N′-dimethylanilinium tetrakis (pentafluorophenyl) borate in toluene (“ABF 20 ”). The molarity of this solution is indicated in the “activation method” of the individual example described below. The solution is heated to approximately 85° C. to dissolve the reagent.
  • the “group 13 reagent” solution is either a solution of triisobutyl aluminium (“TIBA”) or a solution of trimethylaluminium (“TMA”) or a solution of Modified Methylaluminoxane 3A (from Azko Chemical Inc., Chicago, Ill.) (“MMAO”) or a solution of Polymethylaluminoxane-Improved Process (from Azko Chemical Inc., Chicago, Ill.) (“PMAO”), all “group 13 reagent” solutions were solutions in toluene. The molarity of the solutions used is indicated in the “activation method” of the individual example described below.
  • Method AA To the metal-ligand composition, 20 mole equivalents (per metal precursor) of a 500 mM solution of 1-octene in toluene were added to the metal ligand composition in the 1 mL vial. Then, the appropriate amount of the group 13 reagent solution as a 50 mM solution, containing the indicated equivalents group 13 reagent (per metal precursor) in the specific example, was added to the 1 mL vial. After 45 sec, 1.1 mol equivalents (per metal precursor) of the “activator solution” (2.5 mM) was added to the 1 mL vial.
  • Method BB similar to Method AA except the concentration of the activator solution was 5 mM.
  • Method CC To the metal-ligand composition, the appropriate amount of the group 13 reagent solution as a 50 mM solution, containing the indicated equivalents group 13 reagent (per metal precursor) in the specific example, was added to the 1 mL vial. After 40 sec, the indicated amount of the “activator solution” (2.5 mM) was added to the 1 mL vial.
  • Method DD To the metal-ligand composition, the appropriate amount of the group 13 reagent solution (50 mM), containing the indicated equivalents group 13 reagent (per metal precursor) in the specific example, was added to the 1 mL vial that was kept at 50-60° C. After about 10 min, the indicated amount of the “activator solution” (2.5 mM) was added to the 1 mL vial.
  • the polymerization reaction was allowed to continue for 60-900 seconds, during which time the temperature and pressure were maintained at their pre-set levels by computer control.
  • the specific polymerization times for each polymerization are shown in Tables 1-3.
  • the reaction was quenched by addition of an overpressure of carbon dioxide sent to the reactor.
  • the polymerization times were the lesser of the maximum desired polymerization time or the time taken for a predetermined amount of monomer gas to be consumed in the polymerization reaction.
  • the glass vial insert containing the polymer product and solvent, was removed from the pressure cell and removed from the inert atmosphere dry box, and the volatile components were removed using a centrifuge vacuum evaporator. After most of the volatile components had evaporated, the vial contents were dried thoroughly by evaporation at elevated temperature under reduced pressure. The vial was then weighed to determine the yield of polymer product. The polymer product was then analyzed by rapid GPC, as described above to determine the molecular weight of the polymer produced, and by FTIR spectroscopy to determine the crystallinity index. The melting point of selected samples was measured by DSC, as described above.
  • the “Activator Solution” is Either a Solution of N,N′-dimethylanilinium tetrakis (pentafluorophenyl) borate in toluene (“ABF 20 ”) or a solution of tris(pentafluorophenyl) borane in toluene (“BF 15 ”).
  • ABSF 20 Solution of N,N′-dimethylanilinium tetrakis (pentafluorophenyl) borate in toluene
  • BF 15 a solution of tris(pentafluorophenyl) borane in toluene
  • the “ABF 20 ” solution is heated to approximately 85° C. to dissolve the reagent.
  • the molarity is indicated in the “activation method” of the individual example described below.
  • the “group 13 reagent” solution is either a solution of triisobutyl aluminium (“TIBA”) or a solution of trimethylaluminium (“TMA”) or a solution of triethylaluminium (“TEAL”) or a solution of diisobuthylaluminium hydride (“DIBAL”) or a solution of Modified Methylaluminoxane 3A (Azko Chemical Inc., Chicago, Ill.) (“MMAO”) or a solution of Polymethylaluminoxane-Improved Process (Azko Chemical Inc., Chicago, Ill.) (“PMAO”), all “group 13 reagent” solutions were solutions in toluene. The molarity of the solutions used is indicated in the “activation method” of the individual example described below.
  • Method II An appropriate amount of a 0.050M solution of the group 13 reagent, containing the indicated equivalents group 13 reagent (per isolated complex) in the specific examples in Table 4, is dispensed into a 1 mL vial. An appropriate amount complex solution (3-4 mM in dichloroethylene) containing 0.4 umol metal complex is added. After 10 min, 0.44 umol of the activator solution in toluene (2.5 mM) was added to the 1 mL vial.
  • Method JJ similar to Method II except that the concentration of the group 13 reagent solution was 0.200 M.
  • Method KK similar to Method JJ except that the 1 mL vial was heated to 50-60° C.
  • Method LL 40 uL of the 10 mM complex solution in toluene is dispensed into a 1 mL vial.
  • Ethylene-Styrene or Ethylene-1-Octene copolymerizations using metal-ligand compositions A total of twelve (12) separate ethylene-1-octene copolymerization reactions were performed and thirty-nine (39) separate ethylene-styrene copolymerization reactions were performed as described herein:
  • a pre-weighed glass vial insert and disposable stirring paddle were fitted to each reaction vessel of the reactor.
  • the reactor was then closed, 0.10 mL of a 0.02 M group 13 reagent solution in toluene and 3.8 mL of toluene were injected into each pressure reaction vessel through a valve.
  • the identity of the group 13 reagent solution is MMAO.
  • the temperature was then set to 110° C., and the stirring speed was set to 800 rpm, and the mixture was exposed to ethylene at 100 psi pressure. An ethylene pressure of 100 psi in the pressure cell and the temperature setting were maintained, using computer control, until the end of the polymerization experiment.
  • the “activator solution” is a 5 mM solution of N,N′-dimethylanilinium tetrakis (pentafluorophenyl) borate in toluene (“ABF 20 ”). The solution is heated to approximately 85° C. to dissolve the reagent.
  • the group 13 reagent solution is a solution of Modified Methylaluminoxane—3A (Azko) (“MMAO”) in toluene.
  • Method K An appropriate amount ligand solution (10 mM in toluene) was dispensed in a 1 mL glass vial at a scale of 0.4-0.75 mmol. To the 1 mL glass vial containing the ligand solution was added an equimolar amount of metal precursor solution (10 mM in toluene) to form the metal-ligand composition solution. The reaction mixture was heated to 70-80° C. for 45 min.
  • Method EE To the ligand metal composition (preparation described above), 20 equivalents (per metal precursor equivalent) of a 500 mM solution of 1-octene in toluene was added to the metal ligand composition in the 1 mL vial. Then, the indicated amount of the group 13 reagent solution (50 mM) was added to the 1 mL vial. This mixture was held at room temperature for 60-70 sec, during which time, 0.420 mL of comonomer (styrene or 1-octene) followed immediately by 0.380 mL of toluene, were injected into the prepressurized reaction vessel.
  • comonomer styrene or 1-octene
  • the appropriate amount of the “activator solution” (5 mM) was added to the 1 mL vial. After about 30-40 sec, a fraction of the 1 mL vial contents containing the indicated “catalyst amount injected” were injected into the reaction vessel and was followed immediately by injection of toluene to increase the total volume injected of 0.400-0.500 mL.
  • the polymerization reaction was allowed to continue for 60-600 seconds, during which time the temperature and pressure were maintained at their pre-set levels by computer control.
  • the specific times for each polymerization are shown in tables 5-6.
  • the polymerization times were the lesser of the maximum desired polymerization time or the time taken for a predetermined amount of monomer gas to be consumed in the polymerization reaction.
  • the reaction was quenched by addition of an overpressure of carbon dioxide sent to the reactor.
  • the glass vial insert containing the polymer product and solvent, was removed from the pressure cell and removed from the inert atmosphere dry box, and the volatile components were removed using a centrifuge vacuum evaporator. After substantial evaporation of the volatile components, the vial contents were dried thoroughly by evaporation at elevated temperature under reduced pressure. The vial was then weighed to determine the yield of polymer product. The polymer product was then analyzed by rapid GPC, as described above to determine the molecular weight of the polymer produced, and by FTIR or Raman spectroscopy to determine the comonomer incorporation. Results are presented in the Table 5 for ethylene-styrene copolymerizations and Table 6 for ethylene-1-octene copolymerizations.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Inorganic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Polymers & Plastics (AREA)
  • Medicinal Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Biochemistry (AREA)
  • General Health & Medical Sciences (AREA)
  • Molecular Biology (AREA)
  • Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
  • Pyridine Compounds (AREA)
  • Indole Compounds (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Polymers With Sulfur, Phosphorus Or Metals In The Main Chain (AREA)
  • Polyoxymethylene Polymers And Polymers With Carbon-To-Carbon Bonds (AREA)
US10/421,212 2002-04-24 2003-04-23 Bridged bi-aromatic ligands, catalysts, processes for polymerizing and polymers therefrom Expired - Lifetime US6841502B2 (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
US10/421,212 US6841502B2 (en) 2002-04-24 2003-04-23 Bridged bi-aromatic ligands, catalysts, processes for polymerizing and polymers therefrom
US10/957,036 US7126031B2 (en) 2002-04-24 2004-09-30 Bridged bi-aromatic ligands, catalysts, processes for polymerizing and polymers therefrom
US11/436,145 US7241715B2 (en) 2002-04-24 2006-05-16 Bridged bi-aromatic ligands, catalysts, processes for polymerizing and polymers therefrom
US11/775,095 US7659415B2 (en) 2002-04-24 2007-07-09 Bridged bi-aromatic ligands, catalysts, processes for polymerizing and polymers therefrom

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US37536302P 2002-04-24 2002-04-24
US10/421,212 US6841502B2 (en) 2002-04-24 2003-04-23 Bridged bi-aromatic ligands, catalysts, processes for polymerizing and polymers therefrom

Related Child Applications (1)

Application Number Title Priority Date Filing Date
US10/957,036 Division US7126031B2 (en) 2002-04-24 2004-09-30 Bridged bi-aromatic ligands, catalysts, processes for polymerizing and polymers therefrom

Publications (2)

Publication Number Publication Date
US20040014950A1 US20040014950A1 (en) 2004-01-22
US6841502B2 true US6841502B2 (en) 2005-01-11

Family

ID=29270636

Family Applications (7)

Application Number Title Priority Date Filing Date
US10/421,212 Expired - Lifetime US6841502B2 (en) 2002-04-24 2003-04-23 Bridged bi-aromatic ligands, catalysts, processes for polymerizing and polymers therefrom
US10/421,219 Expired - Lifetime US6869904B2 (en) 2002-04-24 2003-04-23 Bridged bi-aromatic ligands, catalysts, processes for polymerizing and polymers therefrom
US10/421,235 Expired - Lifetime US6897276B2 (en) 2002-04-24 2003-04-23 Bridged bi-aromatic ligands, catalysts, processes for polymerizing and polymers therefrom
US10/957,036 Expired - Lifetime US7126031B2 (en) 2002-04-24 2004-09-30 Bridged bi-aromatic ligands, catalysts, processes for polymerizing and polymers therefrom
US11/034,410 Expired - Lifetime US7030256B2 (en) 2002-04-24 2005-01-12 Bridged bi-aromatic ligands, catalysts, processes for polymerizing and polymers therefrom
US11/436,145 Expired - Lifetime US7241715B2 (en) 2002-04-24 2006-05-16 Bridged bi-aromatic ligands, catalysts, processes for polymerizing and polymers therefrom
US11/775,095 Expired - Lifetime US7659415B2 (en) 2002-04-24 2007-07-09 Bridged bi-aromatic ligands, catalysts, processes for polymerizing and polymers therefrom

Family Applications After (6)

Application Number Title Priority Date Filing Date
US10/421,219 Expired - Lifetime US6869904B2 (en) 2002-04-24 2003-04-23 Bridged bi-aromatic ligands, catalysts, processes for polymerizing and polymers therefrom
US10/421,235 Expired - Lifetime US6897276B2 (en) 2002-04-24 2003-04-23 Bridged bi-aromatic ligands, catalysts, processes for polymerizing and polymers therefrom
US10/957,036 Expired - Lifetime US7126031B2 (en) 2002-04-24 2004-09-30 Bridged bi-aromatic ligands, catalysts, processes for polymerizing and polymers therefrom
US11/034,410 Expired - Lifetime US7030256B2 (en) 2002-04-24 2005-01-12 Bridged bi-aromatic ligands, catalysts, processes for polymerizing and polymers therefrom
US11/436,145 Expired - Lifetime US7241715B2 (en) 2002-04-24 2006-05-16 Bridged bi-aromatic ligands, catalysts, processes for polymerizing and polymers therefrom
US11/775,095 Expired - Lifetime US7659415B2 (en) 2002-04-24 2007-07-09 Bridged bi-aromatic ligands, catalysts, processes for polymerizing and polymers therefrom

Country Status (8)

Country Link
US (7) US6841502B2 (de)
EP (1) EP1501840B1 (de)
JP (1) JP4371305B2 (de)
AT (1) ATE492552T1 (de)
AU (1) AU2003225156A1 (de)
CA (1) CA2483192A1 (de)
DE (1) DE60335459D1 (de)
WO (1) WO2003091262A1 (de)

Cited By (33)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20060052554A1 (en) * 2002-04-24 2006-03-09 Symyx Technologies, Inc. Bridged bi-aromatic catalysts, complexes, and methods of using the same
US7091292B2 (en) 2002-04-24 2006-08-15 Symyx Technologies, Inc. Bridged bi-aromatic catalysts, complexes, and methods of using the same
US20060211892A1 (en) * 2002-04-24 2006-09-21 Symyx Technologies, Inc. Bridged bi-aromatic ligands, catalysts, processes for polymerizing and polymers therefrom
US20080255311A1 (en) * 2005-10-31 2008-10-16 Chang Andy C Propylene-Based Elastomeric Composition
US20100184931A1 (en) * 2008-12-31 2010-07-22 Symyx Solutions, Inc. Method for producing very-high or ultra-high molecular weight polyethylene
US20110054122A1 (en) * 2009-08-31 2011-03-03 Jerzy Klosin Catalyst and process for polymerizing an olefin and polyolefin prepared thereby
US20120101241A1 (en) * 2006-05-17 2012-04-26 Harold W Boone ETHYLENE/a-OLEFIN/DIENE SOLUTION POLYMERIZATION PROCESS AND POLYMER
WO2013013116A1 (en) 2011-07-20 2013-01-24 The Procter & Gamble Company Polymer composition
WO2013070601A2 (en) 2011-11-08 2013-05-16 Univation Technologies, Llc Methods of preparing a catalyst system
US20130144018A1 (en) * 2010-08-25 2013-06-06 Dow Global Technologies Llc Process for polymerizing a polymerizable olefin and catalyst therefor
WO2018022279A1 (en) 2016-07-29 2018-02-01 Exxonmobil Chemical Patents Inc. Phenolate transition metal complexes, production and use thereof
WO2018034759A1 (en) 2016-08-15 2018-02-22 Exxonmobil Chemical Patents Inc. Propylene-olefin copolymers and methods for making the same
WO2018034760A1 (en) 2016-08-15 2018-02-22 Exxonmobil Chemical Patents Inc. Propylene-alpha olefin copolymers and methods for making the same
EP3309182A2 (de) 2007-11-15 2018-04-18 Univation Technologies, LLC Polymerisierungskatalysatoren, verfahren zur herstellung und verwendung sowie daraus hergestellte polyolefinprodukte
WO2018089165A1 (en) 2016-11-11 2018-05-17 Exxonmobil Chemical Patents Inc. Catalyst compositions and use thereof
US10023516B2 (en) 2014-12-04 2018-07-17 Dow Technology Investments Llc Hydroformylation process
WO2018191000A1 (en) 2017-04-10 2018-10-18 Exxonmobil Chemicl Patents Inc. Methods for making polyolefin polymer compositions
US10155826B2 (en) 2014-12-12 2018-12-18 Exxonmobil Research And Engineering Company Olefin polymerization catalyst system comprising mesoporous organosilica support
US10221260B2 (en) 2016-07-29 2019-03-05 Exxonmobil Chemical Patents Inc. Phenolate transition metal complexes, production and use thereof
US10280234B2 (en) 2016-11-11 2019-05-07 Exxonmobil Chemical Patents Inc. Catalyst compositions and use thereof
WO2019210030A1 (en) 2018-04-26 2019-10-31 Exxonmobil Chemical Patents Inc. Non-coordinating anion type activators containing cation having branched alkyl groups
US10766975B2 (en) 2016-07-28 2020-09-08 Exxonmobil Chemical Patents Inc. Catalyst compositions and use thereof
WO2021119089A1 (en) 2019-12-11 2021-06-17 Exxonmobil Chemical Patents Inc. Processes for introduction of liquid activators in olefin polymerization reactions
WO2021194831A1 (en) 2020-03-25 2021-09-30 Exxonmobil Chemical Patents Inc. Alkylation of transition metal coordination catalyst complexes
WO2021247244A2 (en) 2020-06-03 2021-12-09 Exxonmobil Chemical Patents Inc. Process for production of thermoplastic vulcanizates using supported catalyst systems and compositions made therefrom
WO2021262838A1 (en) 2020-06-26 2021-12-30 Exxonmobil Chemical Patents Inc. Copolymers composed of ethylene, a-olefin, non-conjugated diene, and substituted styrene and articles therefrom
WO2022035484A1 (en) 2020-08-10 2022-02-17 Exxonmobil Chemical Patents Inc. Methods for delivery of non-aromatic solutions to polymerization reactors
WO2022240946A1 (en) 2021-05-14 2022-11-17 Exxonmobil Chemical Patents Inc. Ethylene-propylene branched copolymers used as viscosity modifiers
US11739169B2 (en) 2020-04-24 2023-08-29 Exxonmobil Chemical Patents Inc. Solubility improvement of non-metallocene transition metal complexes in aliphatic hydrocarbon solvents
WO2025117273A1 (en) 2023-12-01 2025-06-05 ExxonMobil Technology and Engineering Company Support-bound activators, supported catalyst systems, and processes for use thereof
US12466902B2 (en) 2019-08-02 2025-11-11 Exxonmobil Chemical Patents Inc. Non-coordinating anion type activators for use with polyolefin polymerization catalysts
US12503665B2 (en) 2021-05-14 2025-12-23 Exxonmobil Chemical Patents Inc. Ethylene-propylene branched copolymers as viscosity modifiers
US12503529B2 (en) 2021-02-26 2025-12-23 Exxonmobil Chemical Patents Inc. Polymers of 4-substituted hexadiene and processes for production thereof

Families Citing this family (246)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE10130229A1 (de) * 2001-06-22 2003-01-02 Celanese Ventures Gmbh Non-Metallocene, Verfahren zur Herstellung von diesen und deren Verwendung zur Polymerisation von Olefinen
WO2005029037A2 (en) * 2003-09-17 2005-03-31 3M Innovative Properties Company Selective modulation of tlr gene expression
EP2221329B1 (de) 2004-03-17 2014-11-26 Dow Global Technologies LLC Katalysatorzusammensetzung mit einem Ketten-Übertragungsreagens zur Herstellung von Ethylen-Multiblockcopolymeren
BRPI0508173B1 (pt) 2004-03-17 2016-03-15 Dow Global Technologies Inc copolímeros em multibloco, polímero, copolímero, um derivado funcional, mistura homogênea de polímero, processo para a preparação de um copolímero em multibloco contendo propileno e processo para preparar um copolímero em multibloco contendo 4-metil-1-penteno
US8273826B2 (en) 2006-03-15 2012-09-25 Dow Global Technologies Llc Impact modification of thermoplastics with ethylene/α-olefin interpolymers
CA2562090C (en) * 2004-04-29 2014-12-02 Symyx Technologies, Inc. Bridged bi-aromatic catalysts, complexes, and methods of using the same
JP2008509277A (ja) * 2004-08-09 2008-03-27 ダウ グローバル テクノロジーズ インコーポレイティド ポリマーの製造のための担持ビス（ヒドロキシアリールアリールオキシ）触媒
US20060147671A1 (en) * 2004-11-23 2006-07-06 Bemis Peter F Banding apparatus and method of manufacture
US7705157B2 (en) 2004-12-16 2010-04-27 Symyx Solutions, Inc. Phenol-heterocyclic ligands, metal complexes, and their uses as catalysts
US7067451B1 (en) * 2004-12-17 2006-06-27 Fina Technology, Inc. Soluble magnesium complexes useful for the production of polyolefin catalysts and catalysts prepared therewith
ZA200707878B (en) 2005-03-17 2009-06-24 Dow Global Technologies Inc Anti-blocking compositions comprising interpolymers of ethylene/alpha-olefins
US7910658B2 (en) 2005-03-17 2011-03-22 Dow Global Technologies Llc Compositions of ethylene/α-olefin multi-block interpolymer for elastic films and laminates
US8287949B2 (en) * 2005-07-07 2012-10-16 Dow Global Technologies Inc. Aqueous dispersions
US7660581B2 (en) * 2005-09-14 2010-02-09 Jumptap, Inc. Managing sponsored content based on usage history
JP5411502B2 (ja) 2005-09-15 2014-02-12 ダウ グローバル テクノロジーズ エルエルシー 重合性シャトリング剤による接触オレフィンブロック共重合体
US8053529B2 (en) * 2005-09-15 2011-11-08 Dow Global Technologies Llc Catalytic olefin block copolymers with controlled block sequence distribution
AR058448A1 (es) 2005-09-15 2008-02-06 Dow Global Technologies Inc Control de arquitectura del polimero y distribucoin de peso molecular va el agente de transferencia multi- centrado
EP1931686B1 (de) 2005-09-28 2012-08-01 Dow Global Technologies LLC Verfahren zur polymerisation niedermolekularer olefine mit hoher aktivität
WO2007051115A2 (en) 2005-10-26 2007-05-03 Dow Global Technologies Inc. Multi-layer, elastic articles
AU2006329980A1 (en) * 2005-12-16 2007-07-05 Dow Global Technologies Inc. Polydentate heteroatom ligand containing metal complexes, catalysts and methods of making and using the same
EP2018390B1 (de) * 2006-05-05 2016-03-09 Dow Global Technologies LLC Orthometallierte hafniumkomplexe aus imidazolliganden
US8785531B2 (en) * 2006-07-06 2014-07-22 Dow Global Technologies Llc Dispersions of olefin block copolymers
BRPI0714747A2 (pt) * 2006-09-06 2013-05-14 Dow Global Technologies Inc pano entrelaÇado , roupa , fibra apropriada para artigos tÊxteis , artigo entrelaÇado empenado e artigo entrelaÇado circular
WO2008033197A2 (en) * 2006-09-14 2008-03-20 Exxonmobil Chemical Patents Inc. Cyclic olefin copolymers, and methods of making the same
US8476326B2 (en) * 2006-09-22 2013-07-02 Dow Global Technologies Llc Fibrillated polyolefin foam
BRPI0716697A2 (pt) * 2006-11-01 2014-02-25 Dow Global Technologies Inc Composição, artigo, estrutura laminada, artigo moldao, dispersão, artigo moldado, dispersão, artigo por injeção, peça automotiva e adesivo
CN101595252A (zh) * 2006-11-30 2009-12-02 陶氏环球技术公司 用于厚重弹力织物的烯烃嵌段组合物
AU2007325015A1 (en) * 2006-11-30 2008-06-05 Dow Global Technologies Inc. Fabric comprising elastic fibres of cross-linked ethylene polymer
US7842627B2 (en) * 2006-11-30 2010-11-30 Dow Global Technologies Inc. Olefin block compositions for stretch fabrics with wrinkle resistance
US8242237B2 (en) 2006-12-20 2012-08-14 Exxonmobil Chemical Patents Inc. Phase separator and monomer recycle for supercritical polymerization process
EP2094739B1 (de) 2006-12-21 2021-05-19 Dow Global Technologies LLC Polyolefinzusammensetzungen und daraus hergestellte artikel sowie herstellungsverfahren dafür
KR101373926B1 (ko) * 2007-01-16 2014-03-12 다우 글로벌 테크놀로지스 엘엘씨 올레핀 블록 중합체의 신축성 포 및 가먼트
ATE508217T1 (de) * 2007-01-16 2011-05-15 Dow Global Technologies Llc Farbfeste fasern und kleidungsstücke aus olefinblockzusammensetzungen
BRPI0806194A2 (pt) 2007-01-16 2011-08-30 Dow Global Technologies Inc fio tingido em cone
WO2008109628A1 (en) * 2007-03-07 2008-09-12 Dow Global Technologies Inc. Tethered supported transition metal complex
WO2008134186A1 (en) * 2007-04-24 2008-11-06 Dow Global Technologies Inc. THERMOFORMING, SCRATCH-RESISTANT, LOW GLOSS COMPOSITIONS COMPRISING INTERPOLYMERS OF ETHYLENE/α-OLEFINS
BRPI0812613A2 (pt) * 2007-07-09 2019-02-19 Dow Global Technologies Inc fibra adequada para artigos têxteis, composição adequada para fibras e pano
EP2170993B1 (de) 2007-07-13 2019-05-15 Dow Global Technologies LLC Katalytische olefinblockcopolymere mit gesteuerter blocksequenzverteilung und mindestens einem harten block mit niedriger kristallinität
SG183028A1 (en) * 2007-07-13 2012-08-30 Dow Global Technologies Inc Ethylene/a-olefin interpolymers containing low crystallinity hard blocks
WO2009012153A1 (en) * 2007-07-13 2009-01-22 Dow Global Technologies Inc. Viscosity index improver for lubricant compositions
EP2179013B1 (de) * 2007-07-13 2016-04-13 Dow Global Technologies LLC Schmierölzusammensetzungen
CN101878265A (zh) * 2007-09-28 2010-11-03 陶氏环球技术公司 具有改善热变形温度的热塑性烯烃组合物
WO2011087520A1 (en) * 2009-12-22 2011-07-21 Univation Technologies, Llc Catalyst systems having a tailored hydrogen response
ES2435568T3 (es) * 2007-11-19 2013-12-20 Dow Global Technologies Llc Copolímeros de propileno-alfa-olefina con ramificación de cadena larga
ES2682264T3 (es) * 2008-02-29 2018-09-19 Dow Global Technologies Llc Películas orientadas que comprenden un interpolímero de bloques de etileno/alfa-olefina
SG191685A1 (en) * 2008-06-18 2013-07-31 Dow Global Technologies Inc Processes to control fouling and improve compositions
US8372930B2 (en) * 2008-06-20 2013-02-12 Exxonmobil Chemical Patents Inc. High vinyl terminated propylene based oligomers
US8399725B2 (en) 2008-06-20 2013-03-19 Exxonmobil Chemical Patents Inc. Functionalized high vinyl terminated propylene based oligomers
US8283428B2 (en) * 2008-06-20 2012-10-09 Exxonmobil Chemical Patents Inc. Polymacromonomer and process for production thereof
US8802797B2 (en) 2008-06-20 2014-08-12 Exxonmobil Chemical Patents Inc. Vinyl-terminated macromonomer oligomerization
US8283419B2 (en) 2008-06-20 2012-10-09 Exxonmobil Chemical Patents Inc. Olefin functionalization by metathesis reaction
EP2401324B1 (de) 2009-02-25 2013-08-21 Dow Global Technologies LLC Phylonverfahren zur herstellung von schaumstoffartikeln, umfassend ethylen/ -olefin-blockmischpolymere
CN102459357B (zh) 2009-06-05 2013-07-31 陶氏环球技术有限责任公司 制备乙烯的长链支化的(lcb)嵌段共聚物或互连共聚物的方法
US8722817B2 (en) 2009-06-05 2014-05-13 Dow Global Technologies Llc Process to make long chain branched (LCB), block, or interconnected copolymers of ethylene
US9243087B2 (en) 2009-06-11 2016-01-26 Dow Global Technologies Llc LDPE enabling high output and good optics when blended with other polymers
US8318874B2 (en) * 2009-06-26 2012-11-27 Dow Global Technologies Llc Process of selectively polymerizing ethylene and catalyst therefor
US20110003940A1 (en) 2009-07-01 2011-01-06 Dow Global Technologies Inc. Ethylene-based polymer compositions for use as a blend component in shrinkage film applications
WO2011109563A2 (en) * 2010-03-02 2011-09-09 Dow Global Technologies Llc Ethylene-based polymer compositions
WO2011002998A1 (en) 2009-07-01 2011-01-06 Dow Global Technologies Inc. Ethylenic polymer and its use
US8629214B2 (en) 2009-07-01 2014-01-14 Dow Global Technologies Llc. Ethylene-based polymer compositions for use as a blend component in shrinkage film applications
CN106939057B (zh) 2009-07-01 2021-04-23 陶氏环球技术有限责任公司 乙烯类聚合物及其用途
BR112012001942B1 (pt) 2009-07-29 2019-10-22 Dow Global Technologies Llc agente de permuta de cadeia multifuncional, processo para preparar um agente de permuta de cadeia multifuncional, processo para preparar uma composição multifuncional, composição multifuncional, processo para preparar um agente de permuta de cadeia multifuncional contendo poli-radical poliolefina, poliolefina telequélica, processo para preparar uma poliolefina com funcionalidade terminal e separador de bateria
EP3243846B1 (de) 2009-07-29 2021-01-06 Dow Global Technologies LLC Mehrendige kettenübertragungsreagenzien und deren verwendung zur herstellung von blockcopolymeren
KR101769633B1 (ko) 2009-08-10 2017-08-18 다우 글로벌 테크놀로지스 엘엘씨 수축 필름 용도에서 블렌드 성분으로서 사용하기 위한 ｌｄｐｅ
US8598276B2 (en) 2009-09-14 2013-12-03 Dow Global Technologies Llc Polymers comprising units derived from ethylene and poly(alkoxide)
JP5745524B2 (ja) 2009-09-14 2015-07-08 ダウ グローバル テクノロジーズ エルエルシー エチレンおよびポリアルケン由来の単位を含むポリマー
KR101715435B1 (ko) 2009-09-14 2017-03-10 다우 글로벌 테크놀로지스 엘엘씨 에틸렌 및 실록산으로부터 유도된 단위를 포함하는 중합체
KR101470532B1 (ko) * 2009-12-23 2014-12-08 에스케이이노베이션 주식회사 새로운 전이금속 촉매계 및 이를 이용한 에틸렌 단독중합체 또는 에틸렌과 α-올레핀의 공중합체 제조방법
JP2013515823A (ja) 2009-12-24 2013-05-09 ダウ グローバル テクノロジーズ エルエルシー ポリマー組成物、その作製方法、及びそれから調製される物品
CN102822180B (zh) 2010-02-19 2016-06-15 陶氏环球技术有限责任公司 金属配体配合物和催化剂
SG183310A1 (en) 2010-02-19 2012-09-27 Dow Global Technologies Llc Process for polymerizing an olefin monomer and catalyst therefor
CN102906129B (zh) 2010-05-17 2015-02-25 陶氏环球技术有限责任公司 选择性聚合乙烯的方法及其催化剂
JP2013528950A (ja) 2010-06-04 2013-07-11 ダウ グローバル テクノロジーズ エルエルシー 均質ポリオレフィンコポリマーおよび接着性増強グラフトポリマーの膜を含む電子素子モジュール
US20130233383A1 (en) 2010-06-04 2013-09-12 John A. Naumovitz Electronic Device Module Comprising Film of Homogeneous Polyolefin Copolymer and Grafted Silane
EP2591154A2 (de) 2010-07-06 2013-05-15 Ticona GmbH Polyethylenfasern und -membranen von hohem molekulargewicht sowie ihre herstellung und verwendung
US9212234B2 (en) 2010-07-06 2015-12-15 Ticona Gmbh Process for producing high molecular weight polyethylene
JP2013529720A (ja) 2010-07-06 2013-07-22 ティコナ ゲゼルシャフト ミット ベシュレンクテル ハフツング 成形高分子量ポリエチレン物品、それらの製造及び使用
KR20130089165A (ko) * 2010-07-06 2013-08-09 티코나 게엠베하 초고분자량 폴리에틸렌, 및 이의 제조 방법 및 용도
JP2013529718A (ja) * 2010-07-06 2013-07-22 ティコナ ゲゼルシャフト ミット ベシュレンクテル ハフツング 高分子量ポリエチレンの製造方法
EP2591017B1 (de) 2010-07-06 2015-09-09 Ticona GmbH Verfahren zur herstellung von polyethylen mit ultrahohem molekulargewicht
US9034999B2 (en) 2010-07-06 2015-05-19 Ticona Gmbh Process for producing high molecular weight polyethylene
MX346921B (es) 2010-11-02 2017-04-05 Dow Global Technologies Llc Una composicion selladora, metodo para producir la misma.
WO2012061706A1 (en) 2010-11-04 2012-05-10 Dow Global Technologies Llc Double shuttling of polyolefin polymeryl chains
RU2459835C2 (ru) * 2010-11-18 2012-08-27 Учреждение Российской академии наук Институт катализа им. Г.К. Борескова Сибирского отделения РАН Каталитическая система и способ получения реакторного порошка сверхвысокомолекулярного полиэтилена для сверхвысокопрочных сверхвысокомодульных изделий методом холодного формования
SG190985A1 (en) 2010-12-03 2013-07-31 Dow Global Technologies Llc Processes to prepare ethylene-based polymer compositions
SG191203A1 (en) 2010-12-21 2013-07-31 Dow Global Technologies Llc Olefin-based polymers and dispersion polymerizations
EP2658920B1 (de) 2010-12-30 2020-02-12 Dow Global Technologies LLC Zusammensetzungen, verfahren zu ihrer herstellung und daraus hergestellte artikel
KR101843217B1 (ko) 2010-12-30 2018-03-28 다우 글로벌 테크놀로지스 엘엘씨 열가소성 가황 조성물, 이의 제조 방법 및 이로부터 제조된 물품
US8455597B2 (en) 2011-03-25 2013-06-04 Exxonmobil Chemical Patents Inc. Catalysts and methods of use thereof to produce vinyl terminated polymers
US8841397B2 (en) 2011-03-25 2014-09-23 Exxonmobil Chemical Patents Inc. Vinyl terminated higher olefin polymers and methods to produce thereof
US8669326B2 (en) 2011-03-25 2014-03-11 Exxonmobil Chemical Patents Inc. Amine functionalized polyolefin and methods for preparation thereof
US8785562B2 (en) 2011-03-25 2014-07-22 Exxonmobil Chemical Patents Inc. Amphiphilic block polymers prepared by alkene metathesis
US8501894B2 (en) 2011-03-25 2013-08-06 Exxonmobil Chemical Patents Inc. Hydrosilyation of vinyl macromers with metallocenes
US8623974B2 (en) 2011-03-25 2014-01-07 Exxonmobil Chemical Patents Inc. Branched vinyl terminated polymers and methods for production thereof
US8835563B2 (en) 2011-03-25 2014-09-16 Exxonmobil Chemical Patents Inc. Block copolymers from silylated vinyl terminated macromers
US8669330B2 (en) 2011-03-25 2014-03-11 Exxonmobil Chemical Patents Inc. Olefin triblock polymers via ring-opening metathesis polymerization
US8940839B2 (en) 2011-03-25 2015-01-27 Exxonmobil Chemical Patents Inc. Diblock copolymers prepared by cross metathesis
US8426659B2 (en) 2011-03-25 2013-04-23 Exxonmobil Chemical Patents Inc. Vinyl terminated higher olefin polymers and methods to produce thereof
US8399724B2 (en) 2011-03-25 2013-03-19 Exxonmobil Chemical Patents Inc. Vinyl terminated higher olefin copolymers and methods to produce thereof
KR101212637B1 (ko) 2011-06-09 2012-12-14 에스케이종합화학 주식회사 신규한 사이클로펜타［ｂ］플루오레닐 전이금속 화합물, 이를 포함하는 전이금속 촉매 조성물, 및 이를 이용한 에틸렌 단독중합체 또는 에틸렌과 α-올레핀의 공중합체의 제조방법
EP2753663B1 (de) 2011-09-07 2020-01-08 Dow Silicones Corporation Zirkoniumhaltiger komplex und kondensationsreaktionskatalysatoren, verfahren zur herstellung der katalysatoren und zusammensetzungen mit den katalysatoren
CN103781823B (zh) 2011-09-07 2016-08-17 道康宁公司 含钛络合物和缩合反应催化剂、制备该催化剂的方法以及包含该催化剂的组合物
KR101916986B1 (ko) 2011-09-07 2018-11-08 다우 글로벌 테크놀로지스 엘엘씨 중합체 조성물 및 그로부터 제조된 제품
US9139699B2 (en) 2012-10-04 2015-09-22 Dow Corning Corporation Metal containing condensation reaction catalysts, methods for preparing the catalysts, and compositions containing the catalysts
CN103975013B (zh) 2011-10-10 2016-06-01 陶氏环球技术有限责任公司 在机械和热应力下具有改进的保留性能的聚合物组合物
KR101928604B1 (ko) * 2011-10-20 2018-12-12 다우 글로벌 테크놀로지스 엘엘씨 에틸렌계 중합체 조성물 및 그로부터 제조된 물품
KR101858787B1 (ko) 2011-10-24 2018-05-16 미쯔비시 케미컬 주식회사 열가소성 엘라스토머 조성물 및 그 제조 방법
US8604148B2 (en) 2011-11-29 2013-12-10 Exxonmobil Chemical Patents Inc. Functionalization of vinyl terminated polymers by ring opening cross metathesis
BR112014013521A8 (pt) 2011-12-19 2017-06-13 Ticona Gmbh processo para a produção de polietileno, pó de polietileno; e artigo poroso
JP6189325B2 (ja) * 2011-12-20 2017-08-30 ダウ グローバル テクノロジーズ エルエルシー エチレン／アルファオレフィン／非共役ポリエン共重合体およびその形成方法
JP6188715B2 (ja) * 2011-12-29 2017-08-30 ダウ グローバル テクノロジーズ エルエルシー 低分子量エチレン系材料及びアルファ−オレフィン系材料を製造するためのプロセス
US8796376B2 (en) 2012-03-26 2014-08-05 Exxonmobil Chemical Patents Inc. Functionalized polymers and oligomers
CN104271620B (zh) 2012-05-09 2017-07-18 陶氏环球技术有限责任公司 聚烯烃聚合方法、由该方法制造的半结晶基于乙烯的聚合物以及由该聚合物制造的制品
US20150337062A1 (en) * 2012-12-27 2015-11-26 Dow Global Technologies Llc Ethylene Based Polymer
ES2720207T3 (es) 2012-12-27 2019-07-18 Dow Global Technologies Llc Un proceso de polimerización para producir polímeros a base de etileno
BR112015015550B1 (pt) 2012-12-27 2021-05-11 Dow Global Technologies Llc processo de polimerização para a produção de polímeros a base de etileno
US9751998B2 (en) * 2012-12-27 2017-09-05 Dow Global Technologies Llc Catalyst systems for olefin polymerization
JP6175146B2 (ja) * 2013-01-18 2017-08-02 ダウ グローバル テクノロジーズ エルエルシー 高分子量ポリオレフィンのための重合プロセス
CN104968668B (zh) 2013-02-08 2017-11-17 三井化学株式会社 固体状聚铝氧烷组合物、烯烃聚合用催化剂、烯烃聚合物的制造方法及固体状聚铝氧烷组合物的制造方法
CN107266402A (zh) 2013-06-05 2017-10-20 尤尼威蒂恩技术有限责任公司 保护酚基
CN105283474A (zh) 2013-06-28 2016-01-27 陶氏环球技术有限责任公司 使用卤化双苯基苯氧基催化剂控制聚烯烃的分子量
US9063420B2 (en) 2013-07-16 2015-06-23 Rohm And Haas Electronic Materials Llc Photoresist composition, coated substrate, and method of forming electronic device
US9410016B2 (en) 2013-07-16 2016-08-09 Dow Global Technologies Llc Aromatic polyacetals and articles comprising them
US8962779B2 (en) 2013-07-16 2015-02-24 Dow Global Technologies Llc Method of forming polyaryl polymers
US8933239B1 (en) 2013-07-16 2015-01-13 Dow Global Technologies Llc Bis(aryl)acetal compounds
FR3012145B1 (fr) 2013-10-18 2015-12-18 Yriel Procede continu de preparation d'acides boroniques et de leurs derives
CN103804403B (zh) * 2014-02-24 2016-05-18 蚌埠中实化学技术有限公司 一种制备2-羟基苯硼酸的方法
CN103896974B (zh) * 2014-04-11 2017-01-04 北京乐威泰克医药技术有限公司 2-羟基苯硼酸的制备方法
KR102521433B1 (ko) 2014-07-24 2023-04-14 다우 글로벌 테크놀로지스 엘엘씨 저분자량 에틸렌계 폴리머의 중합용 비스-바이페닐페녹시 촉매
KR102569866B1 (ko) * 2014-12-04 2023-08-24 다우 글로벌 테크놀로지스 엘엘씨 에틸렌계 폴리머의 제조용 5개-배위 비스-페닐페녹시 촉매
SG11201705166WA (en) 2014-12-23 2017-07-28 Dow Global Technologies Llc Thermoplastic vulcanizate including a block composite
EP3237475B1 (de) 2014-12-23 2019-01-30 Dow Global Technologies LLC Thermoplastisches vulkanisat mit kautschukblockinterpolymer
EP3285923B1 (de) * 2015-04-20 2019-07-17 Univation Technologies, LLC Verbrückte bi-aromatische liganden und daraus hergestellte olefinpolymerisierungskatalysatoren
CN107531632A (zh) * 2015-04-20 2018-01-02 尤尼威蒂恩技术有限责任公司 用于制备桥连联芳香基配位体的方法
US10252967B2 (en) * 2015-04-20 2019-04-09 Univation Technologies, Llc Bridged bi-aromatic ligands and transition metal compounds prepared therefrom
US10689314B2 (en) * 2015-04-20 2020-06-23 Univation Technologies, Llc Methods for preparing bridged bi-aromatic ligands
WO2016209807A1 (en) 2015-06-22 2016-12-29 Dow Global Technologies Llc Process for making ethylene-based polymers using carbon-carbon free radical initiators
BR112017027521B1 (pt) 2015-06-30 2022-01-04 Dow Global Technologies Llc Processo de polimerização para produzir polímeros à base de etileno
KR102588243B1 (ko) 2015-06-30 2023-10-13 다우 글로벌 테크놀로지스 엘엘씨 에틸렌계 폴리머를 제조하는 중합 방법
ES2925720T3 (es) 2015-09-30 2022-10-19 Dow Global Technologies Llc Un proceso de polimerización para producir polímeros a base de etileno
CN108350121B (zh) 2015-09-30 2021-10-01 陶氏环球技术有限责任公司 主催化剂和使用其的聚合方法
CA3003170C (en) 2015-10-29 2023-09-12 Dow Global Technologies Llc Crosslinkable polymeric compositions for flexible crosslinked cable insulation and methods for making flexible crosslinked cable insulation
US20200270432A1 (en) 2015-12-15 2020-08-27 Dow Global Technologies Llc Cross-linked foams made from interpolymers of ethylene/alpha-olefins
CN109641989B (zh) 2016-07-13 2022-05-03 埃克森美孚化学专利公司 双金属茂催化剂共聚物组合物
WO2018013284A2 (en) 2016-07-13 2018-01-18 Exxonmobil Chemical Patents Inc. Dual metallocene catalyst copolymer compositions
EP3484931A1 (de) 2016-07-14 2019-05-22 ExxonMobil Chemical Patents Inc. Doppelmetallocenkatalysierte bimodale copolymerzusammensetzungen
WO2018022238A1 (en) * 2016-07-28 2018-02-01 Exxonmobile Chemical Patents Inc. Catalyst compositions and use thereof
US11008412B2 (en) 2016-09-29 2021-05-18 Dow Global Technologies Llc Method of polymerizing an olefin
KR102449456B1 (ko) 2016-09-29 2022-10-11 다우 글로벌 테크놀로지스 엘엘씨 개질된 지글러-나타 (전)촉매 및 시스템
TW201840572A (zh) 2016-09-30 2018-11-16 美商陶氏全球科技有限責任公司 適用於鏈梭移之多頭或雙頭組合物及其製備方法
EP4435013A3 (de) 2016-09-30 2024-12-25 Dow Global Technologies LLC Verfahren zur herstellung von mehr- oder doppelköpfigen zusammensetzungen für kettenübertragung
TWI756272B (zh) 2016-09-30 2022-03-01 美商陶氏全球科技有限責任公司 適用於鏈梭移之封端多頭或雙頭組合物及其製備方法
CN109843938B (zh) 2016-10-27 2022-09-30 尤尼威蒂恩技术有限责任公司 制备分子催化剂的方法
CN110114363B (zh) 2017-01-06 2023-01-20 尤尼威蒂恩技术有限责任公司 苯甲基氧基苯氧基酚配体的合成
US10519095B2 (en) 2017-01-06 2019-12-31 Univation Technologies, Llc Synthesis of benzylanilinyl phenyl phenol ligands
US10807998B2 (en) 2017-01-13 2020-10-20 Exxonmobil Chemical Patents Inc. Bridged bis(indenyl) transitional metal complexes, production, and use thereof
CN110612315B (zh) 2017-03-15 2022-08-26 陶氏环球技术有限责任公司 用于形成多嵌段共聚物的催化剂体系
CN110582518B (zh) 2017-03-15 2022-08-09 陶氏环球技术有限责任公司 用于形成多嵌段共聚物的催化剂体系
US20200247936A1 (en) 2017-03-15 2020-08-06 Dow Global Technologies Llc Catalyst system for multi-block copolymer formation
KR102710284B1 (ko) 2017-03-15 2024-09-27 다우 글로벌 테크놀로지스 엘엘씨 다중-블록 공중합체 형성을 위한 촉매 시스템
EP3596146B1 (de) 2017-03-15 2023-07-19 Dow Global Technologies LLC Katalysatorsystem für mehrblockcopolymerbildung
WO2018231224A1 (en) 2017-06-14 2018-12-20 Exxonmobil Chemical Patents Inc. Ethylene copolymer blends for cross-linking applications
WO2018236738A1 (en) 2017-06-20 2018-12-27 Dow Global Technologies Llc Biaryl phenoxy group iv transition metal catalysts for olefin polymerization
ES2890681T3 (es) 2017-06-20 2022-01-21 Dow Global Technologies Llc Catalizadores de biaril-fenoxi-metal de transición del grupo IV para la polimerización de olefinas
US10544244B2 (en) 2017-08-02 2020-01-28 Exxonmobil Chemical Patents Inc. Bridged biphenyl phenol transition metal complexes, production and use thereof
CN111164110A (zh) * 2017-09-29 2020-05-15 陶氏环球技术有限责任公司 在金属上具有烷氧基或酰胺基配体的用于改进溶解度的双-苯基-苯氧基聚烯烃催化剂
KR102590976B1 (ko) 2017-09-29 2023-10-19 다우 글로벌 테크놀로지스 엘엘씨 개선된 용해도를 위한 금속 상에 메틸렌트리알킬규소 리간드를 갖는 비스-페닐-페녹시 폴리올레핀 촉매
EP3688042B1 (de) 2017-09-29 2023-11-22 Dow Global Technologies LLC Bis-phenyl-phenoxy-polyolefin-katalysatoren mit zwei methylentrialkylsiliciumliganden auf dem metall für verbesserte löslichkeit
BR112020012842B1 (pt) 2017-12-26 2024-01-02 Dow Global Technologies Llc Método para produzir um polímero trimodal em um processo de polimerização em solução
KR102605947B1 (ko) 2017-12-26 2023-11-28 다우 글로벌 테크놀로지스 엘엘씨 다봉형 에틸렌계 중합체의 제조를 위한 이중 반응기 용액 공정
EP3732214B1 (de) 2017-12-26 2023-11-01 Dow Global Technologies LLC Zusammensetzungen mit multimodalen ethylenbasierten polymeren mit verbesserter zähigkeit bei niedrigen temperaturen
CN111683979B (zh) 2017-12-26 2024-08-23 陶氏环球技术有限责任公司 用于生产多峰型乙烯类聚合物的工艺
ES2908893T3 (es) 2017-12-26 2022-05-04 Dow Global Technologies Llc Composiciones poliméricas a base de etileno multimodales con tenacidad mejorada
EP3732217B1 (de) 2017-12-26 2023-06-21 Dow Global Technologies, LLC Zusammensetzungen mit auf multimodalem ethylen basierenden polymeren und polyethylen mit niedriger dichte (ldpe)
WO2019156968A1 (en) 2018-02-07 2019-08-15 Exxonmobil Chemical Patents Inc. Supported catalysts systems and polymerization processes for using the same
JP2021518463A (ja) 2018-03-19 2021-08-02 ダウ グローバル テクノロジーズ エルエルシー シリコン終端化有機金属化合物およびそれを調製するためのプロセス
JP7364585B2 (ja) 2018-03-30 2023-10-18 ダウ グローバル テクノロジーズ エルエルシー オレフィン重合のための二核助触媒としての高溶解性ビスホウ酸
JP2021519362A (ja) 2018-03-30 2021-08-10 ダウ グローバル テクノロジーズ エルエルシー オレフィン重合活性化剤
EP3774941B1 (de) 2018-03-30 2022-11-02 Dow Global Technologies LLC Binukleare olefinpolymerisierungsaktivatoren
US11787880B2 (en) 2018-03-30 2023-10-17 Dow Global Technologies Llc Highly soluble alkyl substituted carbenium borate as co-catalysts for olefin polymerizations
US11447586B2 (en) 2018-03-30 2022-09-20 Dow Global Technologies Llc Olefin polymerization activators
CN112292417B (zh) 2018-06-15 2023-10-13 陶氏环球技术有限责任公司 包括具有高分子量高密度级分的双峰型乙烯类聚合物的吹塑膜
US11873393B2 (en) 2018-06-15 2024-01-16 Dow Global Technologies Llc Bimodal ethylene-based polymers having high molecular weight high density fractions
MY205150A (en) 2018-06-15 2024-10-03 Dow Global Technologies Llc Cast films comprising bimodal ethylene-based polymers having high molecular weight high density fractions
SG11202012176XA (en) 2018-06-15 2021-01-28 Dow Global Technologies Llc Process for the production of bimodal ethylene-based polymers having high molecular weight high density fractions
US10927134B2 (en) 2018-08-28 2021-02-23 Exxonmobil Chemical Patents Inc. Bridged phenolate transition metal complexes, production, and uses thereof
WO2020046597A1 (en) 2018-08-29 2020-03-05 Exxonmobil Chemical Patents Inc. Methods of making polymer compositions with enhanced elasticity by employing vtp and hmp catalyst systems in parallel processes
JP7460602B2 (ja) 2018-08-30 2024-04-02 ダウ グローバル テクノロジーズ エルエルシー ２つのアントラセニル配位子を有するビス－フェニル－フェノキシポリオレフィンプロ触媒
WO2020069086A2 (en) 2018-09-27 2020-04-02 Exxonmobil Chemical Patents Inc. C1,c2-bridged ligands and catalysts
TWI839414B (zh) 2018-11-30 2024-04-21 美商陶氏全球科技有限責任公司 具有平衡特性之基於聚合物之膜
KR102881199B1 (ko) 2018-12-20 2025-11-06 다우 글로벌 테크놀로지스 엘엘씨 사슬 이동 능력을 가진 비아릴 하이드록시티오펜 iv족 전이금속 중합 촉매
EP3898723A1 (de) 2018-12-20 2021-10-27 Dow Global Technologies LLC Biarylphenoxygruppe-iv-übergangsmetallkatalysatoren für die olefinpolymerisation
KR102916971B1 (ko) 2018-12-28 2026-01-23 다우 글로벌 테크놀로지스 엘엘씨 텔레켈릭 폴리올레핀 및 이의 제조 방법
US12180314B2 (en) 2018-12-28 2024-12-31 Dow Global Technologies Llc Curable compositions comprising unsaturated polyolefins
CN113412264B (zh) 2018-12-28 2024-06-25 陶氏环球技术有限责任公司 有机金属链转移剂
CN113498414A (zh) 2018-12-28 2021-10-12 陶氏环球技术有限责任公司 包括遥爪聚烯烃的可固化组合物
CA3125275A1 (en) 2018-12-28 2020-07-02 Dow Global Technologies Llc Curable compositions comprising unsaturated polyolefins
JP7242879B2 (ja) * 2019-02-12 2023-03-20 エクソンモービル ケミカル パテンツ インコーポレイテッド 遷移金属ビス（フェノレート）錯体およびオレフィン重合のための触媒としてのその使用
US11248070B2 (en) 2019-02-12 2022-02-15 Exxonmobil Chemical Patents Inc. Lewis base catalysts and methods thereof
US11214634B2 (en) 2019-02-12 2022-01-04 Exxonmobil Chemical Patents Inc. Lewis base catalysts and methods thereof
SG11202108010RA (en) * 2019-02-12 2021-08-30 Exxonmobil Chemical Patents Inc Lewis base catalysts and methods thereof
WO2020167819A1 (en) * 2019-02-12 2020-08-20 Exxonmobil Chemical Patents Inc. Lewis base catalysts and methods thereof
US11225539B2 (en) 2019-02-12 2022-01-18 Exxonmobil Chemical Patents Inc. Supported transition metal bis(phenolate) complexes and their use as catalysts for olefin polymerization
USD966445S1 (en) * 2019-02-13 2022-10-11 Global Sports Innovation LTD Sports training device
WO2020184421A1 (ja) 2019-03-12 2020-09-17 三井化学株式会社 オレフィン系樹脂、その架橋物およびそれらの製造方法
WO2020198196A1 (en) 2019-03-28 2020-10-01 Dow Global Technologies Llc Anionic group iii complexes as weakly coordinating anions for olefin polymerization catalyst activators
CN113795523B (zh) 2019-04-30 2024-03-08 陶氏环球技术有限责任公司 烯烃官能化活化剂
WO2021035709A1 (en) 2019-08-30 2021-03-04 Dow Global Technologies Llc Polyolefin compositions having improved electrical properties
JP7679370B2 (ja) * 2019-11-04 2025-05-19 ダウ グローバル テクノロジーズ エルエルシー チタンビフェニルフェノール重合触媒
CN111072698B (zh) * 2019-12-28 2022-06-14 沧州普瑞东方科技有限公司 一种羟基苯硼酸的制备方法
KR20230065372A (ko) 2020-01-31 2023-05-11 다우 글로벌 테크놀로지스 엘엘씨 Iii족 및 란타나이드 비스-페닐-페녹시 금속-리간드 착물
KR20220137683A (ko) 2020-01-31 2022-10-12 다우 글로벌 테크놀로지스 엘엘씨 Iii족 및 란타나이드 비스-페닐-페녹시 금속-리간드 착물 및 사슬 이동제를 포함하는 중합 공정
JP7684981B2 (ja) * 2020-02-11 2025-05-28 エクソンモービル ケミカル パテンツ インコーポレイテッド 遷移金属ビス（フェノラート）触媒錯体を用いて得られるプロピレンコポリマー及びその生成のための均一プロセス
KR20220152223A (ko) * 2020-02-11 2022-11-15 엑손모빌 케미칼 패턴츠 인코포레이티드 전이 금속 비스(페놀레이트) 촉매 복합체를 사용하여 얻은 프로필렌 중합체 및 그의 균질한 제조 방법
US20230287156A1 (en) * 2020-02-11 2023-09-14 Exxonmobil Chemical Patents Inc. Polyethylene Compositions Obtained Using Transition Metal Bis(Phenolate) Catalyst Complexes and Homogeneous Process for Production Thereof
CN115315455A (zh) * 2020-02-11 2022-11-08 埃克森美孚化学专利公司 使用过渡金属双(酚盐)催化剂络合物获得的乙烯-α-烯烃-二烯单体共聚物及生产该共聚物的均相方法
TWI874791B (zh) 2020-02-18 2025-03-01 美商基利科學股份有限公司 抗病毒化合物
TWI794742B (zh) 2020-02-18 2023-03-01 美商基利科學股份有限公司 抗病毒化合物
AU2021224588B2 (en) 2020-02-18 2024-07-18 Gilead Sciences, Inc. Antiviral compounds
US11732063B2 (en) 2020-02-24 2023-08-22 Exxonmobil Chemical Patents Inc. Lewis base catalysts and methods thereof
EP4126995B1 (de) * 2020-03-24 2024-09-11 Nova Chemicals (International) S.A. Polymerisationskatalysator mit einem tetradentaten liganden
US12497472B2 (en) 2020-03-27 2025-12-16 Dow Global Technologies Llc Long-chain branched ethylene-based polymers
BR112022019374A2 (pt) 2020-03-27 2022-11-16 Dow Global Technologies Llc Processo para polimerizar polímeros à base de etileno
CN115279805B (zh) 2020-03-27 2025-01-03 陶氏环球技术有限责任公司 长链支化的基于乙烯的聚合物
US20230128663A1 (en) 2020-03-27 2023-04-27 Dow Global Technologies Llc Long-chain branched ethylene-based polymers
EP4127061A1 (de) 2020-03-30 2023-02-08 ExxonMobil Chemical Patents Inc. Kammblockcopolymere und verfahren dafür
CN111747976B (zh) * 2020-06-30 2023-07-14 万华化学(四川)有限公司 一种金属配合物及其制备方法与应用
CN116234834A (zh) 2020-07-17 2023-06-06 陶氏环球技术有限责任公司 双苯基苯氧基金属-配体络合物的烃基改性甲基铝氧烷助催化剂
US20240010771A1 (en) 2020-07-17 2024-01-11 Dow Global Technologies Llc Hydrocarbyl-modified methylaluminoxane cocatalyst for bis-phenylphenoxy metal-ligand complexes
US20240010770A1 (en) 2020-07-17 2024-01-11 Dow Global Technologies Llc Hydrocarbyl-modified methylaluminoxane cocatalysts for bis-phenylphenoxy metal-ligand complexes
US11738334B2 (en) 2020-08-11 2023-08-29 Exxonmobil Chemical Patents Inc. Supported catalyst systems and processes for use thereof
JP7629985B2 (ja) 2020-08-13 2025-02-14 エクソンモービル ケミカル パテンツ インコーポレイテッド 遷移金属ビス（フェノラート）触媒錯体を使用して得られる環含有ポリマー組成物およびその製造方法
EP4222180B1 (de) 2020-09-30 2024-04-10 ExxonMobil Chemical Patents Inc. Bis(heterocyclisches-olat) lewis-base-katalysatoren und verfahren dafür
JP2023552277A (ja) 2020-11-10 2023-12-15 ダウ グローバル テクノロジーズ エルエルシー ポリエチレンの表面エネルギーを増加させるためのポリオレフィン－ポリアクリレートブロックコポリマー添加剤の調製
WO2022103803A1 (en) 2020-11-10 2022-05-19 Dow Global Technologies Llc Preparation of non-polar–polar block copolymers via vinyl-terminated polyolefins
KR20230110334A (ko) * 2020-11-23 2023-07-21 사빅 글로벌 테크놀러지스 비.브이. 관능화 폴리올레핀의 제조를 위한 용액 공정
US20230399425A1 (en) * 2020-11-23 2023-12-14 Sabic Global Technologies B.V. Solution process for production of halide- or tertiary amine- functionalized polyolefins
US20230303597A1 (en) * 2020-12-28 2023-09-28 Sabic Sk Nexlene Company Pte. Ltd. Metal-ligand complex, catalyst composition for preparing ethylene-based polymer containing the same, and preparation method of ethylene -based polymer using the same
ES3031808T3 (en) * 2021-02-26 2025-07-11 Dow Global Technologies Llc Bis-phenoxy-ether ligands for group iv polyolefin catalysis
JP7688152B2 (ja) 2021-04-16 2025-06-03 ギリアード サイエンシーズ， インコーポレイテッド アミドを使用してカルバヌクレオシドを調製する方法
JP7719954B2 (ja) 2021-08-18 2025-08-06 ギリアード サイエンシーズ， インコーポレイテッド リン脂質化合物並びにその製造方法及び使用方法
CN117999292A (zh) 2021-09-10 2024-05-07 陶氏环球技术有限责任公司 用于烯烃聚合的烃溶性硼酸盐助催化剂
EP4512834A3 (de) 2021-09-10 2025-05-14 Dow Global Technologies LLC Borat-cokatalysatoren für die polyolefinherstellung
EP4644434A1 (de) 2022-12-28 2025-11-05 Kuraray Co., Ltd. 3-methyl-1-buten-basiertes polymer, herstellungsverfahren dafür, harzzusammensetzung, pellet und formkörper
CN121693523A (zh) 2023-08-28 2026-03-17 陶氏环球技术有限责任公司 包含消费后再循环（pcr）基于乙烯的聚合物的聚合物共混物
WO2025188486A1 (en) 2024-03-05 2025-09-12 ExxonMobil Technology and Engineering Company Polyolefin catalysts and methods thereof

Citations (43)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4297465A (en) 1980-10-29 1981-10-27 Eastman Kodak Company Catalysts for polymerizing propylene in a high temperature solution process
EP0277004A1 (de) 1987-01-30 1988-08-03 Exxon Chemical Patents Inc. Katalysatoren, Verfahren zur Herstellung derselben und Verfahren zu deren Anwendung
EP0292134A2 (de) 1987-05-04 1988-11-23 Shell Oil Company Herstellung eines Katalysatorbestandteils zur Olefinpolymerisation
US4971936A (en) 1989-07-10 1990-11-20 Shell Oil Company Catalyst component for making primarily isotactic elastomeric polypropylene or polybutene
US5064802A (en) 1989-09-14 1991-11-12 The Dow Chemical Company Metal complex compounds
US5093415A (en) 1987-05-19 1992-03-03 Union Carbide Chemicals & Plastics Technology Corporation Process for producing stereoregular polymers having a narrow molecular weight distribution
US5153157A (en) 1987-01-30 1992-10-06 Exxon Chemical Patents Inc. Catalyst system of enhanced productivity
EP0534405A1 (de) 1991-09-24 1993-03-31 Union Carbide Chemicals & Plastics Technology Corporation Verfahren zur Verlangsamung oder Beendung der Polymerisation
EP0582194A1 (de) 1992-08-03 1994-02-09 Hoechst Aktiengesellschaft Verfahren zur Herstellung eines Olefinpolymers unter Verwendung von Metallocenen mit speziell substituierten Indenylliganden
WO1994007926A1 (en) 1992-09-25 1994-04-14 Shell Oil Company Process for polymerizing alpha-olefin
WO1994011409A1 (en) 1992-11-06 1994-05-26 Shell Oil Company Process for polymerizing alpha-olefin
US5318935A (en) 1990-12-27 1994-06-07 Exxon Chemical Patents Inc. Amido transition metal compound and a catalyst system for the production of isotatic polypropylene
EP0622380A1 (de) 1993-04-29 1994-11-02 Montell North America Inc. Kristalline Propylenpolymere, die eine hohe Schmelzflussrate und eine enge Molekulargewichtsverteilung aufweisen
US5385993A (en) 1991-02-27 1995-01-31 Mitsubishi Petrochemical Company Limited Production of olefin polymers
US5453410A (en) 1992-01-06 1995-09-26 The Dow Chemical Company Catalyst composition
JPH08217775A (ja) 1995-02-08 1996-08-27 Takasago Internatl Corp 新規クラウンチオエーテル及びその遷移金属錯体並びにこれを用いる光学活性アルコールの製造方法
US5599761A (en) 1987-01-30 1997-02-04 Exxon Chemical Patents, Inc. Ionic metallocene catalyst compositions
US5616664A (en) 1994-08-02 1997-04-01 The Dow Chemical Company Polymerization process with biscyclopentadienyl diene complex containing catalysts
WO1998003521A1 (en) 1996-07-23 1998-01-29 Symyx Technologies Combinatorial synthesis and analysis of organometallic compounds and catalysts
WO1999005186A1 (en) 1997-07-27 1999-02-04 Technion Research And Development Foundation Ltd. PROCESS FOR THE PRODUCTION OF STEREOREGULAR POLYMERS AND ELASTOMERS OF α-OLEFINS AND CERTAIN NOVEL CATALYSTS THEREFOR
WO1999006413A1 (en) 1997-08-01 1999-02-11 The Dow Chemical Company Catalyst activator
EP0922712A1 (de) 1997-12-10 1999-06-16 Union Carbide Chemicals & Plastics Technology Corporation Neuen Elektronendonor enthaltende Zusammensetzungen
WO1999042467A1 (en) 1998-02-20 1999-08-26 The Dow Chemical Company Catalyst activators comprising expanded anions
US5985356A (en) 1994-10-18 1999-11-16 The Regents Of The University Of California Combinatorial synthesis of novel materials
WO2000009255A2 (en) 1998-08-13 2000-02-24 Symyx Technologies Parallel reactor with internal sensing and method of using same
US6030917A (en) 1996-07-23 2000-02-29 Symyx Technologies, Inc. Combinatorial synthesis and analysis of organometallic compounds and catalysts
US6175409B1 (en) 1999-04-02 2001-01-16 Symyx Technologies, Inc. Flow-injection analysis and variable-flow light-scattering methods and apparatus for characterizing polymers
US6214939B1 (en) 1993-08-13 2001-04-10 Mitsui Chemicals Olefin polymerization catalyst and process for preparing polypropylene and propylene block copolymer
US6239236B1 (en) 1997-09-03 2001-05-29 Montell Technology Company B.V. Components and catalysts for the polymerization of olefins
US6260407B1 (en) 1998-04-03 2001-07-17 Symyx Technologies, Inc. High-temperature characterization of polymers
US6262199B1 (en) 1992-07-10 2001-07-17 Fina Technology, Inc. Process and catalyst for producing isotactic polyolefins
US6294388B1 (en) 1998-04-03 2001-09-25 Symyx Technologies, Inc. Indirect calibration of polymer characterization systems
WO2001098371A2 (en) 2000-06-19 2001-12-27 Symyx Technologies, Inc. High throughput screen for identifying polymerization catalysts from potential catalysts
US20020002256A1 (en) 1998-09-16 2002-01-03 Thomas Henry Peterson Catalyst composition for the polymerization of olefins
WO2002002576A1 (en) 2000-06-30 2002-01-10 Exxonmobil Chemical Patents Inc. Bridged bis (indenyl) metallocene compounds
WO2002036638A2 (en) 2000-11-06 2002-05-10 Ramot University Authority For Applied Research & Industrial Development Ltd. Active non-metallocene pre-catalyst and method for tactic catalytic polymerization of alpha-olefin monomers
US6406632B1 (en) 1998-04-03 2002-06-18 Symyx Technologies, Inc. Rapid characterization of polymers
US6436292B1 (en) 1999-04-02 2002-08-20 Symyx Technologies, Inc. Parallel high-performance liquid chromatography with post-separation treatment
US6455316B1 (en) 1998-08-13 2002-09-24 Symyx Technologies, Inc. Parallel reactor with internal sensing and method of using same
JP2002280179A (ja) 2001-03-16 2002-09-27 Canon Inc 有機発光素子
US6491816B2 (en) 1999-04-02 2002-12-10 Symyx Technologies, Inc. Apparatus for parallel high-performance liquid chromatography with serial injection
US6508984B1 (en) 1998-04-03 2003-01-21 Symyx Technologies, Inc. System for creating and testing novel catalysts, reactions and polymers
US6548026B1 (en) 1998-08-13 2003-04-15 Symyx Technologies, Inc. Parallel reactor with internal sensing and method of using same

Family Cites Families (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US626040A (en) * 1899-05-30 John r
US4452914A (en) * 1982-08-13 1984-06-05 The Dow Chemical Company Titanium complexes and catalysts prepared therefrom
JPH08134064A (ja) * 1994-11-10 1996-05-28 Takasago Internatl Corp 新規クラウンチオエーテルおよびその遷移金属錯体並びにこれを用いる不斉ヒドロシリル化方法
DE4442556C2 (de) * 1994-11-30 1999-05-27 Danfoss As Hydraulische Axialkolbenmaschine
US6759014B2 (en) * 2001-01-26 2004-07-06 Symyx Technologies, Inc. Apparatus and methods for parallel processing of multiple reaction mixtures
US6380392B1 (en) 1999-06-30 2002-04-30 The Penn State Research Foundation Ligands based on chiral 2-amino-2′-hydroxy-1,1′-binaphthyl and related frameworks for asymmetric catalysis
FR2802833B1 (fr) 1999-12-24 2002-05-10 Inst Francais Du Petrole Composition catalytique et procede pour l'oligomerisation de l'ethylene, en particulier en hexene-1
US6455648B1 (en) 1999-12-29 2002-09-24 Chevron Phillips Chemical Company Lp Olefin production
WO2002038628A2 (en) * 2000-11-07 2002-05-16 Symyx Technologies, Inc. Substituted pyridyl amine ligands, complexes and catalysts therefrom; processes for producing polyolefins therewith
WO2002083306A2 (en) 2001-04-12 2002-10-24 Sasol Technology (Pty) Ltd Oligomerisation process and catalyst system
WO2002085820A2 (en) 2001-04-20 2002-10-31 Indiana University Chiral organic compounds and metal coordination complexes thereof
US7060848B2 (en) * 2002-04-24 2006-06-13 Symyx Technologies, Inc. Bridged bi-aromatic catalysts, complexes, and methods of using the same
US6841502B2 (en) 2002-04-24 2005-01-11 Symyx Technologies, Inc. Bridged bi-aromatic ligands, catalysts, processes for polymerizing and polymers therefrom
US7091292B2 (en) * 2002-04-24 2006-08-15 Symyx Technologies, Inc. Bridged bi-aromatic catalysts, complexes, and methods of using the same
CA2562090C (en) 2004-04-29 2014-12-02 Symyx Technologies, Inc. Bridged bi-aromatic catalysts, complexes, and methods of using the same

Patent Citations (49)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4297465A (en) 1980-10-29 1981-10-27 Eastman Kodak Company Catalysts for polymerizing propylene in a high temperature solution process
US5599761A (en) 1987-01-30 1997-02-04 Exxon Chemical Patents, Inc. Ionic metallocene catalyst compositions
US5153157A (en) 1987-01-30 1992-10-06 Exxon Chemical Patents Inc. Catalyst system of enhanced productivity
EP0277004A1 (de) 1987-01-30 1988-08-03 Exxon Chemical Patents Inc. Katalysatoren, Verfahren zur Herstellung derselben und Verfahren zu deren Anwendung
EP0292134A2 (de) 1987-05-04 1988-11-23 Shell Oil Company Herstellung eines Katalysatorbestandteils zur Olefinpolymerisation
US5093415A (en) 1987-05-19 1992-03-03 Union Carbide Chemicals & Plastics Technology Corporation Process for producing stereoregular polymers having a narrow molecular weight distribution
US4971936A (en) 1989-07-10 1990-11-20 Shell Oil Company Catalyst component for making primarily isotactic elastomeric polypropylene or polybutene
US5064802A (en) 1989-09-14 1991-11-12 The Dow Chemical Company Metal complex compounds
US5318935A (en) 1990-12-27 1994-06-07 Exxon Chemical Patents Inc. Amido transition metal compound and a catalyst system for the production of isotatic polypropylene
US5385993A (en) 1991-02-27 1995-01-31 Mitsubishi Petrochemical Company Limited Production of olefin polymers
EP0534405A1 (de) 1991-09-24 1993-03-31 Union Carbide Chemicals & Plastics Technology Corporation Verfahren zur Verlangsamung oder Beendung der Polymerisation
US5453410A (en) 1992-01-06 1995-09-26 The Dow Chemical Company Catalyst composition
US6262199B1 (en) 1992-07-10 2001-07-17 Fina Technology, Inc. Process and catalyst for producing isotactic polyolefins
EP0582194A1 (de) 1992-08-03 1994-02-09 Hoechst Aktiengesellschaft Verfahren zur Herstellung eines Olefinpolymers unter Verwendung von Metallocenen mit speziell substituierten Indenylliganden
WO1994007926A1 (en) 1992-09-25 1994-04-14 Shell Oil Company Process for polymerizing alpha-olefin
WO1994011409A1 (en) 1992-11-06 1994-05-26 Shell Oil Company Process for polymerizing alpha-olefin
EP0622380A1 (de) 1993-04-29 1994-11-02 Montell North America Inc. Kristalline Propylenpolymere, die eine hohe Schmelzflussrate und eine enge Molekulargewichtsverteilung aufweisen
US6214939B1 (en) 1993-08-13 2001-04-10 Mitsui Chemicals Olefin polymerization catalyst and process for preparing polypropylene and propylene block copolymer
US5616664A (en) 1994-08-02 1997-04-01 The Dow Chemical Company Polymerization process with biscyclopentadienyl diene complex containing catalysts
US5985356A (en) 1994-10-18 1999-11-16 The Regents Of The University Of California Combinatorial synthesis of novel materials
JPH08217775A (ja) 1995-02-08 1996-08-27 Takasago Internatl Corp 新規クラウンチオエーテル及びその遷移金属錯体並びにこれを用いる光学活性アルコールの製造方法
WO1998003521A1 (en) 1996-07-23 1998-01-29 Symyx Technologies Combinatorial synthesis and analysis of organometallic compounds and catalysts
US6030917A (en) 1996-07-23 2000-02-29 Symyx Technologies, Inc. Combinatorial synthesis and analysis of organometallic compounds and catalysts
WO1999005186A1 (en) 1997-07-27 1999-02-04 Technion Research And Development Foundation Ltd. PROCESS FOR THE PRODUCTION OF STEREOREGULAR POLYMERS AND ELASTOMERS OF α-OLEFINS AND CERTAIN NOVEL CATALYSTS THEREFOR
WO1999006413A1 (en) 1997-08-01 1999-02-11 The Dow Chemical Company Catalyst activator
US6239236B1 (en) 1997-09-03 2001-05-29 Montell Technology Company B.V. Components and catalysts for the polymerization of olefins
EP0922712A1 (de) 1997-12-10 1999-06-16 Union Carbide Chemicals & Plastics Technology Corporation Neuen Elektronendonor enthaltende Zusammensetzungen
WO1999042467A1 (en) 1998-02-20 1999-08-26 The Dow Chemical Company Catalyst activators comprising expanded anions
US6406632B1 (en) 1998-04-03 2002-06-18 Symyx Technologies, Inc. Rapid characterization of polymers
US6260407B1 (en) 1998-04-03 2001-07-17 Symyx Technologies, Inc. High-temperature characterization of polymers
US6508984B1 (en) 1998-04-03 2003-01-21 Symyx Technologies, Inc. System for creating and testing novel catalysts, reactions and polymers
US6294388B1 (en) 1998-04-03 2001-09-25 Symyx Technologies, Inc. Indirect calibration of polymer characterization systems
US6491823B1 (en) 1998-04-03 2002-12-10 Symyx Technologies, Inc. Targeted separation protocols for rapid characterizations of polymers
US6475391B2 (en) 1998-04-03 2002-11-05 Symyx Technologies, Inc. Rapid characterization of polymers for combinatorial, analytical and process control applications
US6461515B1 (en) 1998-04-03 2002-10-08 Symyx Technologies, Inc. Parallel liquid chromatography for analyzing combinatorial libraries of non-biological polymers
US6454947B1 (en) 1998-04-03 2002-09-24 Symyx Technologies, Inc. Overlaid injection for rapid characterizations of polymers
WO2000009255A2 (en) 1998-08-13 2000-02-24 Symyx Technologies Parallel reactor with internal sensing and method of using same
US6455316B1 (en) 1998-08-13 2002-09-24 Symyx Technologies, Inc. Parallel reactor with internal sensing and method of using same
US6489168B1 (en) 1998-08-13 2002-12-03 Symyx Technologies, Inc. Analysis and control of parallel chemical reactions
US6306658B1 (en) 1998-08-13 2001-10-23 Symyx Technologies Parallel reactor with internal sensing
US6548026B1 (en) 1998-08-13 2003-04-15 Symyx Technologies, Inc. Parallel reactor with internal sensing and method of using same
US20020002256A1 (en) 1998-09-16 2002-01-03 Thomas Henry Peterson Catalyst composition for the polymerization of olefins
US6436292B1 (en) 1999-04-02 2002-08-20 Symyx Technologies, Inc. Parallel high-performance liquid chromatography with post-separation treatment
US6491816B2 (en) 1999-04-02 2002-12-10 Symyx Technologies, Inc. Apparatus for parallel high-performance liquid chromatography with serial injection
US6175409B1 (en) 1999-04-02 2001-01-16 Symyx Technologies, Inc. Flow-injection analysis and variable-flow light-scattering methods and apparatus for characterizing polymers
WO2001098371A2 (en) 2000-06-19 2001-12-27 Symyx Technologies, Inc. High throughput screen for identifying polymerization catalysts from potential catalysts
WO2002002576A1 (en) 2000-06-30 2002-01-10 Exxonmobil Chemical Patents Inc. Bridged bis (indenyl) metallocene compounds
WO2002036638A2 (en) 2000-11-06 2002-05-10 Ramot University Authority For Applied Research & Industrial Development Ltd. Active non-metallocene pre-catalyst and method for tactic catalytic polymerization of alpha-olefin monomers
JP2002280179A (ja) 2001-03-16 2002-09-27 Canon Inc 有機発光素子

Non-Patent Citations (51)

* Cited by examiner, † Cited by third party
Title
Applied Homogeneous Catalysis, Wiley-VCH, edited by B. Cornils and W.A. Herrmann: 2nd Ed. 2002 vol. 1, 213-273.
Applied Homogeneous Catalysis, Wiley-VCH, edited by B. Cornils and W.A. Herrmann: 2nd Ed., 2002 vol. 2, 740-747.
Arrowsmith et al., "Comparison Of The Polymerization Of Propene By Homogeneous And Heterogeneous Metallocene/MAO-Catalysts Under Different Polymerization Conditions," Macromol. Chem. Phys. 2001, 202, 2161-2167.
Bennett et al., "Catalytic Conjugate Addition Promoted By The Copper(<1>)-monothiobinaphthol System. Part 3. <1 >Comparison Of Three Thiolate-based Catalytic Systems," J. Chem. Soc., Perkin Trans. 1, 1999, 3127-3132.
Bennett et al., "Catalytic Conjugate Addition Promoted By The Copper(1)-monothiobinaphthol System. Part 3. 1 Comparison Of Three Thiolate-based Catalytic Systems," J. Chem. Soc., Perkin Trans. 1, 1999, 3127-3132.
Bochmann et al., "Base-Free Cationic Zirconium Benzyl Complexes As Highly Active Polymerization Catalysts," Organometallics, 1993, 12, 633-640.
Brintzinger, et al., "Stereospecific Olefin Polymerization with Chiral Metallocene Catalysts", Angew. Chem. Int., Ed. Engl., 1995, vol. 34, pp. 1143-1170.
Britovsek, et al., "The Search For New-Generation Olefin Polymerization Catalysts: Life Beyond Metallocenes," Angew. Chem. Int. Ed. 1999, 38, 428-447.
Chang et al., "Syntheses of New Lactones Containing Phenyl or Methyl Groups", Kongop Hwahak, J. of Korean Ind. & Eng. Chemistry, vol. 9, No. 6, 1998, 842-845.
Chemical Reviews, 2000, 100, No. 4, "Frontiers in Metal-Catalyzed Polymerization" Entire issue.
Chen, et al., "Cocatalysts For Metal-Catalyzed Olefin Polymerization: Activators, Activation Processes, and Structure-Activity Relationships," Chem. Rev. 2000, 100, 1391-1434.
Coates, "Precise Control of Polyolefin Stereochemistry Using Single-Site Metal Catalysts," Chem. Rev. 2000, 100, 1223-1252.
Cram et al., J. Am. Chem. Soc., vol. 103, 1981, pp. 6228-6232, XP002245914-The Whole Document.
Cram et al., J. Am. Chem. Soc., vol. 107, 1985, pp. 3645-3657, XP002245917-The Whole Document.
Cram et al., J. Am. Chem. Soc., vol. 107, 1985, pp. 3657-3668, XP002245916-The Whole Document.
Cram et al., J. Chem. Soc., Chem. Comm., No. 21, 1979, pp. 948-950, XP009012986-The Whole Document.
Cram et al., J. Chem. Soc., Chem. Commun., No. 5, 1982, pp. 301-304, XP009012987-The Whole Document.
Cram et al., J. Org. Chem., vol. 50, 1985, pp. 1486-1496, XP002245918-The Whole Document.
Cram et al., J. Org. Chem., vol. 54, 1989, pp. 5460-5482, XP002245915-The Whole Document.
Deng et al., "Synthesis Of High-Melting, Isotactic Polypropene With C2- and C1-Symmentrical Zirconocenes," Macromolecules 1996, 29, 6371-6376.
Ewen et al., "Evaluation Of The Dimethylsilyl-Bis(2-Methyl-4-Phenyl-1-Indenyl) Ligand With Group 4 Triad Metals In Propene Polymerizations With Methylaluminoxane," Macromol. Rapid Commun., 1998, 19, 71-73.
Fink et al., "Propene Polymerization With Silica-Supported Matallocence/MAO Catalysts," Chem. Rev. 2000, 100, 1377-1390.
Gibson et al., "Advances in Non-Metallocence Olefin Polymerization Catalysis" Chem. Rev. 2003, 103, 283-315.
Helgeson et al., Acta Crystallographica, Section C: Crystal Structure Communications, vol. C56, No. 7, 2000, pp. 795-797, XP009012979-The Whole Document.
Hlatky, "Heterogeneous Single-Site Catalysts For Olefin Polymerization," Chem. Rev. 2000, 100, 1347-1376.
Jordan, "Chemistry of Cationic Dicyclopentadienyl Group 4 Metal-Alkyl Complexes", Adv. Organometallic Chem., 1991, vol. 32, pp. 325-153.
Kaminsky et al., "The Influence Of The Polymerization Process On The Product Properties Of Metallocence-Polypropene," Chem. Eng. Technol., 2001, 24, 11, 1124-1128.
Klapars et al., J. Am. Chem. Soc. 2001, 123(31), 7727-7729.
Knobler et al., Journal of Inclusion Phenomena and Molecular Recognition in Chemistry, vol. 12, No. 1-4, 1992, pp. 341-360, XP009012984-The Whole Document.
Kol et al., J. Am. Chem. Soc. 2000, 122, 43, 10706-10707.
LaPointe, et al., J. Am. Chem. Soc. 2000, 122, 39, 9560-9561.
Luongo, J. Appl. Polym. Sci., 3(1960) 302-309.
Patent Abstracts of Japan, vol. 1996, No. 12, Dec. 26, 1996 & JP 08 217775 A (Takasago Internat'l Corp.), Aug. 27, 1996 (Aug. 27, 1996) Abstract.
Patent Abstracts of Japan, vol. 2003, No. 01, Jan. 14, 2003 & JP 2002 280179 A (Canon Inc.), Sep. 2002 (Sep. 27, 2002) Abstract.
Patent Abstracts of Japan, vol., 1996, No. 09, Sep. 30, 1996 & JUP 08 134064 A (Takasago Internat'l Corp.), May 28, 1996 (May 28, 1996) Astract.
Pellecchia et al., "Single Insertion of alpha-Olefins into The Cationic Complex [Zr(CH2Ph)3]<+> Affording Isolable [Zr(CH2Ph)2(CH2CHRCH2Ph)]<+> Adducts: A Model For the Insertion Mechanism in Ziegler-Natta Polymerization," Organometallics 1994, 13, 298-302.
Pellecchia et al., "Synthesis, Crystal Structure, and Olefin Polymerization Activity of a Zwitterionic eta<6>-Arene Zirconium Tris(hydrocarbyl)," J. Am. Chem. Soc. 1993, 115, 1160-1162.
Pellecchia et al., "Single Insertion of α-Olefins into The Cationic Complex [Zr(CH2Ph)3]+ Affording Isolable [Zr(CH2Ph)2(CH2CHRCH2Ph)]+ Adducts: A Model For the Insertion Mechanism in Ziegler-Natta Polymerization," Organometallics 1994, 13, 298-302.
Pellecchia et al., "Synthesis, Crystal Structure, and Olefin Polymerization Activity of a Zwitterionic η6-Arene Zirconium Tris(hydrocarbyl)," J. Am. Chem. Soc. 1993, 115, 1160-1162.
Pellecchia, et al., "A Novel eta</> Coordination Mode Of A Benzyl Ligand In A Cationic Zirconium Complex," Organometallics 1994, 13, 3773-3775.
Pellecchia, et al., "A Novel η/ Coordination Mode Of A Benzyl Ligand In A Cationic Zirconium Complex," Organometallics 1994, 13, 3773-3775.
Piers, et al. "New Bifunctional Perfluoroaryl Boranes: Synthesis and Reactivity of the ortho-Phenylene-Bridged Diboranes 1,2-(B(C6F5)2)2C6X4 (X=H, F)", J. Am. Chem. Soc., 1999, 121, 3244-3245.
Resconi, et al., "Selectivity In Propene Polymerization With Metallocenc Catalysts," Chem. Rev. 2000, 100, 1253-1345.
Schrock, Organometallics 1999, 18, pp. 3649-3670.
Stanforth, Tetrahedron, 1998, 54(3/4), 263-303.
Sundell, Polymer 37 (1996) 3227-3231.
Takahashi et al., "An Expedient Route To Some Monoalkyl Ethers Of Enantiomerically Pure Bi-beta-napthol," Tetrahedron: Asymmetry, 1997, 8, 18, 3125-3130.
Takahashi et al., "An Expedient Route To Some Monoalkyl Ethers Of Enantiomerically Pure Bi-β-napthol," Tetrahedron: Asymmetry, 1997, 8, 18, 3125-3130.
UEDA et al., J. Chem. Soc., Chem Commun., No. 9, 1995, pp. 935-936, XP009012989-The Whole Document.
Vathauer et al., "Extremely Active Polymerizations Of Propene By Bisindenylzirconocences And Tetra(pentafluorophenyl)-borate," Polymer 2001, 42, 4017-4024.
Walter et al., "Novel Polypropylene Materials," J.M.S.-Pure Appl. Chem., 1999, A36(11), 1613-1639.

Cited By (51)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7241715B2 (en) * 2002-04-24 2007-07-10 Symyx Technologies, Inc. Bridged bi-aromatic ligands, catalysts, processes for polymerizing and polymers therefrom
US7060848B2 (en) 2002-04-24 2006-06-13 Symyx Technologies, Inc. Bridged bi-aromatic catalysts, complexes, and methods of using the same
US7091292B2 (en) 2002-04-24 2006-08-15 Symyx Technologies, Inc. Bridged bi-aromatic catalysts, complexes, and methods of using the same
US20060205588A1 (en) * 2002-04-24 2006-09-14 Symyx Technologies, Inc. Bridged bi-aromatic catalysts, complexes, and methods of using the same
US20060211892A1 (en) * 2002-04-24 2006-09-21 Symyx Technologies, Inc. Bridged bi-aromatic ligands, catalysts, processes for polymerizing and polymers therefrom
US7241714B2 (en) 2002-04-24 2007-07-10 Symyx Technologies, Inc. Bridged bi-aromatic catalysts, complexes, and methods of using the same
US20080269470A1 (en) * 2002-04-24 2008-10-30 Symyx Technologies, Inc. Bridged Bi-Aromatic Ligands, Catalysts, Processes For Polymerizing And Polymers Therefrom
US7659415B2 (en) 2002-04-24 2010-02-09 Symyx Solutions, Inc. Bridged bi-aromatic ligands, catalysts, processes for polymerizing and polymers therefrom
US20060052554A1 (en) * 2002-04-24 2006-03-09 Symyx Technologies, Inc. Bridged bi-aromatic catalysts, complexes, and methods of using the same
US20110118418A1 (en) * 2005-10-31 2011-05-19 Chang Andy C Propylene-Based Elastomeric Composition
US20080255311A1 (en) * 2005-10-31 2008-10-16 Chang Andy C Propylene-Based Elastomeric Composition
US7893161B2 (en) 2005-10-31 2011-02-22 Dow Global Technologies Inc. Propylene-based elastomeric composition
US8022144B2 (en) 2005-10-31 2011-09-20 Dow Global Technologies Llc Propylene-based elastomeric composition
US20120101241A1 (en) * 2006-05-17 2012-04-26 Harold W Boone ETHYLENE/a-OLEFIN/DIENE SOLUTION POLYMERIZATION PROCESS AND POLYMER
US8299189B2 (en) * 2006-05-17 2012-10-30 Dow Global Technologies, Llc Ethylene/α-olefin/diene solution polymerization process and polymer
EP3309182A2 (de) 2007-11-15 2018-04-18 Univation Technologies, LLC Polymerisierungskatalysatoren, verfahren zur herstellung und verwendung sowie daraus hergestellte polyolefinprodukte
US20140121342A1 (en) * 2008-12-31 2014-05-01 Symyx Solutions, Inc. Method for producing very-high or ultra-high molecular weight polyethylene
US20100184931A1 (en) * 2008-12-31 2010-07-22 Symyx Solutions, Inc. Method for producing very-high or ultra-high molecular weight polyethylene
US9175107B2 (en) * 2008-12-31 2015-11-03 Symyx Solutions, Inc. Method for producing very-high or ultra-high molecular weight polyethylene
US8637618B2 (en) * 2008-12-31 2014-01-28 Symyx Solutions, Inc. Method for producing very-high or ultra-high molecular weight polyethylene
US20110054122A1 (en) * 2009-08-31 2011-03-03 Jerzy Klosin Catalyst and process for polymerizing an olefin and polyolefin prepared thereby
CN105294905A (zh) * 2010-08-25 2016-02-03 陶氏环球技术有限责任公司 聚合可聚合烯烃的方法以及用于该方法的催化剂
US20130144018A1 (en) * 2010-08-25 2013-06-06 Dow Global Technologies Llc Process for polymerizing a polymerizable olefin and catalyst therefor
US9029487B2 (en) * 2010-08-25 2015-05-12 Dow Global Technologies Llc Process for polymerizing a polymerizable olefin and catalyst therefor
KR101865645B1 (ko) * 2010-08-25 2018-06-11 다우 글로벌 테크놀로지스 엘엘씨 중합성 올레핀의 중합 방법 및 그를 위한 촉매
WO2013013116A1 (en) 2011-07-20 2013-01-24 The Procter & Gamble Company Polymer composition
WO2013070601A2 (en) 2011-11-08 2013-05-16 Univation Technologies, Llc Methods of preparing a catalyst system
US9234060B2 (en) 2011-11-08 2016-01-12 Univation Technologies, Llc Methods of preparing a catalyst system
US10023516B2 (en) 2014-12-04 2018-07-17 Dow Technology Investments Llc Hydroformylation process
US10155826B2 (en) 2014-12-12 2018-12-18 Exxonmobil Research And Engineering Company Olefin polymerization catalyst system comprising mesoporous organosilica support
US10766975B2 (en) 2016-07-28 2020-09-08 Exxonmobil Chemical Patents Inc. Catalyst compositions and use thereof
WO2018022279A1 (en) 2016-07-29 2018-02-01 Exxonmobil Chemical Patents Inc. Phenolate transition metal complexes, production and use thereof
US10221260B2 (en) 2016-07-29 2019-03-05 Exxonmobil Chemical Patents Inc. Phenolate transition metal complexes, production and use thereof
WO2018034759A1 (en) 2016-08-15 2018-02-22 Exxonmobil Chemical Patents Inc. Propylene-olefin copolymers and methods for making the same
WO2018034760A1 (en) 2016-08-15 2018-02-22 Exxonmobil Chemical Patents Inc. Propylene-alpha olefin copolymers and methods for making the same
US10280234B2 (en) 2016-11-11 2019-05-07 Exxonmobil Chemical Patents Inc. Catalyst compositions and use thereof
WO2018089165A1 (en) 2016-11-11 2018-05-17 Exxonmobil Chemical Patents Inc. Catalyst compositions and use thereof
WO2018191000A1 (en) 2017-04-10 2018-10-18 Exxonmobil Chemicl Patents Inc. Methods for making polyolefin polymer compositions
WO2019210030A1 (en) 2018-04-26 2019-10-31 Exxonmobil Chemical Patents Inc. Non-coordinating anion type activators containing cation having branched alkyl groups
US12466902B2 (en) 2019-08-02 2025-11-11 Exxonmobil Chemical Patents Inc. Non-coordinating anion type activators for use with polyolefin polymerization catalysts
WO2021119089A1 (en) 2019-12-11 2021-06-17 Exxonmobil Chemical Patents Inc. Processes for introduction of liquid activators in olefin polymerization reactions
WO2021194831A1 (en) 2020-03-25 2021-09-30 Exxonmobil Chemical Patents Inc. Alkylation of transition metal coordination catalyst complexes
US12528892B2 (en) 2020-03-25 2026-01-20 Exxonmobil Chemical Patents Inc. Alkylation of transition metal coordination catalyst complexes
US11739169B2 (en) 2020-04-24 2023-08-29 Exxonmobil Chemical Patents Inc. Solubility improvement of non-metallocene transition metal complexes in aliphatic hydrocarbon solvents
WO2021247244A2 (en) 2020-06-03 2021-12-09 Exxonmobil Chemical Patents Inc. Process for production of thermoplastic vulcanizates using supported catalyst systems and compositions made therefrom
WO2021262838A1 (en) 2020-06-26 2021-12-30 Exxonmobil Chemical Patents Inc. Copolymers composed of ethylene, a-olefin, non-conjugated diene, and substituted styrene and articles therefrom
WO2022035484A1 (en) 2020-08-10 2022-02-17 Exxonmobil Chemical Patents Inc. Methods for delivery of non-aromatic solutions to polymerization reactors
US12503529B2 (en) 2021-02-26 2025-12-23 Exxonmobil Chemical Patents Inc. Polymers of 4-substituted hexadiene and processes for production thereof
WO2022240946A1 (en) 2021-05-14 2022-11-17 Exxonmobil Chemical Patents Inc. Ethylene-propylene branched copolymers used as viscosity modifiers
US12503665B2 (en) 2021-05-14 2025-12-23 Exxonmobil Chemical Patents Inc. Ethylene-propylene branched copolymers as viscosity modifiers
WO2025117273A1 (en) 2023-12-01 2025-06-05 ExxonMobil Technology and Engineering Company Support-bound activators, supported catalyst systems, and processes for use thereof

Also Published As

Publication number Publication date
US7659415B2 (en) 2010-02-09
US7241715B2 (en) 2007-07-10
EP1501840A1 (de) 2005-02-02
DE60335459D1 (de) 2011-02-03
JP4371305B2 (ja) 2009-11-25
US20050080281A1 (en) 2005-04-14
US6869904B2 (en) 2005-03-22
US20050164872A1 (en) 2005-07-28
US20060211892A1 (en) 2006-09-21
US7126031B2 (en) 2006-10-24
AU2003225156A1 (en) 2003-11-10
US7030256B2 (en) 2006-04-18
US20040005984A1 (en) 2004-01-08
US20040014950A1 (en) 2004-01-22
US20040010103A1 (en) 2004-01-15
US6897276B2 (en) 2005-05-24
WO2003091262A1 (en) 2003-11-06
US20080269470A1 (en) 2008-10-30
JP2005523921A (ja) 2005-08-11
ATE492552T1 (de) 2011-01-15
EP1501840B1 (de) 2010-12-22
CA2483192A1 (en) 2003-11-06

Similar Documents

Publication Publication Date Title
US7659415B2 (en) Bridged bi-aromatic ligands, catalysts, processes for polymerizing and polymers therefrom
US7241714B2 (en) Bridged bi-aromatic catalysts, complexes, and methods of using the same
US7060848B2 (en) Bridged bi-aromatic catalysts, complexes, and methods of using the same
EP1751169B1 (de) Verbrückte biaromatische katalysatoren, komplexe und verfahren zu deren anwendung
US7642216B2 (en) Methods of using heterocycle-amine ligands, compositions, complexes, and catalysts
US7018949B2 (en) Substituted pyridyl amine catalysts and processes for polymerizing and polymers
US7256296B2 (en) Heterocycle-amine ligands, compositions, complexes, and catalysts
JP6653173B2 (ja) エチレン系ポリマー
US8569532B2 (en) Catalysts
US8394902B2 (en) Pyridyldiamido transition metal complexes, production and use thereof
US20080071046A1 (en) Cyclic olefin copolymers, and methods of making the same
KR20110031995A (ko) 피리딜다이아미도 전이 금속 착체, 이의 제조 및 용도
US20050227860A1 (en) Polymerisation catalyst
US7074870B2 (en) Styrene polymers and phenol-triazole type complexes, catalysts, and processes for polymerizing
WO2007076231A2 (en) Bridged phenol-heterocyclic ligands, metal complexes, and their uses as catalysts

Legal Events

Date Code Title Description
AS Assignment

Owner name: SYMYX TECHNOLOGIES, INC., CALIFORNIA

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:BOUSSIE, THOMAS R.;DIAMOND, GARY M.;LAPOINTE, ANNE M.;AND OTHERS;REEL/FRAME:014318/0909;SIGNING DATES FROM 20030521 TO 20030702

STCF Information on status: patent grant

Free format text: PATENTED CASE

CC Certificate of correction
CC Certificate of correction
FPAY Fee payment

Year of fee payment: 4

AS Assignment

Owner name: SYMYX SOLUTIONS, INC., CALIFORNIA

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:SYMYX TECHNOLOGIES, INC.;REEL/FRAME:022939/0564

Effective date: 20090701

Owner name: SYMYX SOLUTIONS, INC.,CALIFORNIA

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:SYMYX TECHNOLOGIES, INC.;REEL/FRAME:022939/0564

Effective date: 20090701

AS Assignment

Owner name: FREESLATE, INC.,CALIFORNIA

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:SYMYX SOLUTIONS, INC.;REEL/FRAME:024057/0911

Effective date: 20100301

Owner name: FREESLATE, INC., CALIFORNIA

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:SYMYX SOLUTIONS, INC.;REEL/FRAME:024057/0911

Effective date: 20100301

FPAY Fee payment

Year of fee payment: 8

REMI Maintenance fee reminder mailed
AS Assignment

Owner name: DOW GLOBAL TECHNOLOGIES LLC, MICHIGAN

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:FREESLATE, INC.;REEL/FRAME:039758/0949

Effective date: 20160915

FPAY Fee payment

Year of fee payment: 12

SULP Surcharge for late payment

Year of fee payment: 11